WO2020105650A1 - Composition, et corps étiré - Google Patents

Composition, et corps étiré

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Publication number
WO2020105650A1
WO2020105650A1 PCT/JP2019/045334 JP2019045334W WO2020105650A1 WO 2020105650 A1 WO2020105650 A1 WO 2020105650A1 JP 2019045334 W JP2019045334 W JP 2019045334W WO 2020105650 A1 WO2020105650 A1 WO 2020105650A1
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WIPO (PCT)
Prior art keywords
group
mass
less
carbon atoms
polymer
Prior art date
Application number
PCT/JP2019/045334
Other languages
English (en)
Japanese (ja)
Inventor
義典 難波
市川　賢治
陽平 藤本
裕俊 吉田
洋之 佐藤
丈人 加藤
剣吾 伊藤
拓 山中
Original Assignee
ダイキン工業株式会社
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by ダイキン工業株式会社 filed Critical ダイキン工業株式会社
Priority to CN201980075185.3A priority Critical patent/CN113039241B/zh
Priority to US17/294,871 priority patent/US20220010118A1/en
Priority to CN202311349659.3A priority patent/CN117417612A/zh
Priority to EP19886627.9A priority patent/EP3885406A4/fr
Priority to JP2020557572A priority patent/JP7299510B2/ja
Publication of WO2020105650A1 publication Critical patent/WO2020105650A1/fr
Priority to JP2023095792A priority patent/JP2023124874A/ja

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Classifications

    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F2/00—Processes of polymerisation
    • C08F2/04—Polymerisation in solution
    • C08F2/10—Aqueous solvent
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L27/00—Compositions of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Compositions of derivatives of such polymers
    • C08L27/02—Compositions of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Compositions of derivatives of such polymers not modified by chemical after-treatment
    • C08L27/12—Compositions of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Compositions of derivatives of such polymers not modified by chemical after-treatment containing fluorine atoms
    • C08L27/18—Homopolymers or copolymers or tetrafluoroethene
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F14/00—Homopolymers and copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen
    • C08F14/18—Monomers containing fluorine
    • C08F14/26—Tetrafluoroethene
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F214/00—Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen
    • C08F214/18—Monomers containing fluorine
    • C08F214/26—Tetrafluoroethene
    • C08F214/262—Tetrafluoroethene with fluorinated vinyl ethers
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J5/00—Manufacture of articles or shaped materials containing macromolecular substances
    • C08J5/18—Manufacture of films or sheets
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2327/00—Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Derivatives of such polymers
    • C08J2327/02—Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Derivatives of such polymers not modified by chemical after-treatment
    • C08J2327/12—Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Derivatives of such polymers not modified by chemical after-treatment containing fluorine atoms
    • C08J2327/18—Homopolymers or copolymers of tetrafluoroethylene
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2429/00—Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by an alcohol, ether, aldehydo, ketonic, acetal, or ketal radical; Hydrolysed polymers of esters of unsaturated alcohols with saturated carboxylic acids; Derivatives of such polymer
    • C08J2429/10—Homopolymers or copolymers of unsaturated ethers
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2205/00—Polymer mixtures characterised by other features
    • C08L2205/02—Polymer mixtures characterised by other features containing two or more polymers of the same C08L -group
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L27/00—Compositions of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Compositions of derivatives of such polymers
    • C08L27/22—Compositions of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Compositions of derivatives of such polymers modified by chemical after-treatment

Definitions

  • the present disclosure relates to a composition and a stretched body.
  • Patent Document 1 a polymer comprising polymerized units represented by Formula 1, or a polymerized unit represented by Formula 1 and Formula 2 is used.
  • An average aspect characterized by polymerizing tetrafluoroethylene in the presence of a copolymer comprising polymerized units represented is 40 mol% or more.
  • a method for producing an aqueous dispersion containing rod-shaped fine particles of polytetrafluoroethylene having a ratio of 2 or more is described. -CF 2 CFX -...
  • R f is a perfluoroperfluoroalkylene group having 1 to 6 carbon atoms
  • M is an alkali metal ion or an ammonium ion
  • X is a fluorine atom or a chlorine atom.
  • Patent Document 2 describes particles containing a bulk of a fluoropolymer and a core of a fluorinated ionomer.
  • Patent Document 3 is a method for producing an aqueous dispersion of fluoropolymer particles, which comprises a step of providing dispersed fine particles of a fluorinated ionomer in an aqueous polymerization medium, and dispersed fine particles of the fluorinated ionomer in the aqueous polymerization medium. And polymerizing at least one fluorinated monomer in the presence of an initiator to form an aqueous dispersion of particles of fluoropolymer.
  • the present disclosure aims to provide a composition having excellent stretchability.
  • the present disclosure includes polytetrafluoroethylene and a polymer (I) containing a polymerized unit (I) based on a monomer represented by the following general formula (I), and has a standard specific gravity of 2.200 or less.
  • a composition characterized by: CX 1 X 3 CX 2 R (-CZ 1 Z 2 -A 0 ) m (I) (In the formula, X 1 and X 3 are each independently F, Cl, H or CF 3 ; A 0 is an anionic group; X 2 is H, F, an alkyl group or a fluorine-containing group.
  • R is a linking group; Z 1 and Z 2 are each independently H, F, an alkyl group or a fluorine-containing alkyl group; m is an integer of 1 or more.)
  • the composition of the present disclosure preferably has a breaking strength of 10.0 N or more.
  • the composition of the present disclosure preferably has a stress relaxation time of 50 seconds or more.
  • the composition of the present disclosure preferably has an extrusion pressure of 10.0 MPa or more and 30.0 MPa or less.
  • the polytetrafluoroethylene preferably has an endothermic peak temperature in the range of 333 to 347 ° C.
  • the above-mentioned anionic group is a sulfate group, a carboxylate group, a phosphate group, a phosphonate group, a sulfonate group, or -C (CF 3 ) 2 OM (wherein M is -H, a metal atom, -NR 7 4 , It is imidazolium which may have a substituent, pyridinium which may have a substituent or phosphonium which may have a substituent, and R 7 is H or an organic group.). It is preferably an anionic group.
  • the composition of the present disclosure preferably contains substantially no fluorine-containing surfactant.
  • the composition of the present disclosure is preferably a powder.
  • the present disclosure also relates to a stretched body comprising the above composition.
  • R is a linking group; Z 1 and Z 2 are each independently H, F, an alkyl group or a fluorine-containing alkyl group; m is an integer of 1 or more.)
  • the stretched body of the present disclosure preferably has a breaking strength of 10.0 N or more.
  • the stretched body of the present disclosure preferably has a stress relaxation time of 50 seconds or more.
  • the stretched body of the present disclosure preferably has an endothermic peak temperature of 325 to 350 ° C.
  • the above-mentioned anionic group is a sulfate group, a carboxylate group, a phosphate group, a phosphonate group, a sulfonate group, or -C (CF 3 ) 2 OM (wherein M is -H, a metal atom, -NR 7 4 , It is imidazolium which may have a substituent, pyridinium which may have a substituent or phosphonium which may have a substituent, and R 7 is H or an organic group.). It is preferably an anionic group.
  • the stretched product of the present disclosure preferably contains substantially no fluorine-containing surfactant.
  • composition of the present disclosure has excellent stretchability.
  • melt processability means that the polymer can be melted and processed using conventional processing equipment such as extruders and injection molding machines. Therefore, the melt-processable fluororesin usually has a melt flow rate of 0.01 to 500 g / 10 minutes as measured by the measuring method described later.
  • organic group means a group containing one or more carbon atoms, or a group formed by removing one hydrogen atom from an organic compound.
  • Examples of the “organic group” are An alkyl group which may have one or more substituents, An alkenyl group which may have one or more substituents, An alkynyl group which may have one or more substituents, A cycloalkyl group which may have one or more substituents, A cycloalkenyl group which may have one or more substituents, A cycloalkadienyl group which may have one or more substituents, An aryl group which may have one or more substituents, An aralkyl group which may have one or more substituents, A non-aromatic heterocyclic group which may have one or more substituents, A heteroaryl group which may have one or more substituents, Cyano group, Formyl group, RaO-, RaCO-, RaSO 2 ⁇ , RaCOO-, RaNRa
  • substituteduent means a substitutable group.
  • substitutable group examples include an aliphatic group, an aromatic group, a heterocyclic group, an acyl group, an acyloxy group, an acylamino group, an aliphatic oxy group, an aromatic oxy group, a heterocyclic oxy group, an aliphatic oxycarbonyl group.
  • the above-mentioned aliphatic group may be saturated or unsaturated, and a hydroxy group, an aliphatic oxy group, a carbamoyl group, an aliphatic oxycarbonyl group, an aliphatic thio group, an amino group, an aliphatic amino group. It may have an acylamino group, a carbamoylamino group, or the like.
  • the aliphatic group include an alkyl group having a total carbon number of 1 to 8, preferably 1 to 4, such as a methyl group, an ethyl group, a vinyl group, a cyclohexyl group and a carbamoylmethyl group.
  • aromatic group examples include a nitro group, a halogen atom, an aliphatic oxy group, a carbamoyl group, an aliphatic oxycarbonyl group, an aliphatic thio group, an amino group, an aliphatic amino group, an acylamino group and a carbamoylamino group. You may have.
  • the aromatic group is an aryl group having 6 to 12 carbon atoms, preferably 6 to 10 total carbon atoms, for example, phenyl group, 4-nitrophenyl group, 4-acetylaminophenyl group, 4-methanesulfonylphenyl group. And so on.
  • the heterocyclic group has a halogen atom, a hydroxy group, an aliphatic oxy group, a carbamoyl group, an aliphatic oxycarbonyl group, an aliphatic thio group, an amino group, an aliphatic amino group, an acylamino group, a carbamoylamino group, etc. May be.
  • Examples of the above-mentioned heterocyclic group include a 5 to 6-membered heterocyclic ring having a total carbon number of 2 to 12, preferably 2 to 10, such as 2-tetrahydrofuryl group and 2-pyrimidyl group.
  • the acyl group is an aliphatic carbonyl group, an arylcarbonyl group, a heterocyclic carbonyl group, a hydroxy group, a halogen atom, an aromatic group, an aliphatic oxy group, a carbamoyl group, an aliphatic oxycarbonyl group, an aliphatic thio group, an amino group. It may have an aliphatic amino group, an acylamino group, a carbamoylamino group, or the like.
  • the acyl group include an acyl group having a total carbon number of 2 to 8, preferably 2 to 4, such as acetyl group, propanoyl group, benzoyl group, 3-pyridinecarbonyl group.
  • the acylamino group may have an aliphatic group, an aromatic group, a heterocyclic group, or the like, and has, for example, an acetylamino group, a benzoylamino group, a 2-pyridinecarbonylamino group, a propanoylamino group, or the like. May be.
  • a propanoylamino group and the like is the above-mentioned acylamino group.
  • the aliphatic oxycarbonyl group may be saturated or unsaturated, and may be a hydroxy group, an aliphatic oxy group, a carbamoyl group, an aliphatic oxycarbonyl group, an aliphatic thio group, an amino group, an aliphatic group. It may have an amino group, an acylamino group, a carbamoylamino group, or the like.
  • Examples of the aliphatic oxycarbonyl group include alkoxycarbonyl groups having 2 to 8 and preferably 2 to 4 carbon atoms in total, such as methoxycarbonyl group, ethoxycarbonyl group, (t) -butoxycarbonyl group.
  • the carbamoyl group may have an aliphatic group, an aromatic group, a heterocyclic group, or the like.
  • Examples of the carbamoyl group include an unsubstituted carbamoyl group, an alkylcarbamoyl group having 2 to 9 carbon atoms in total, preferably an unsubstituted carbamoyl group, an alkylcarbamoyl group having 2 to 5 carbon atoms in total, such as an N-methylcarbamoyl group, Examples thereof include N, N-dimethylcarbamoyl group and N-phenylcarbamoyl group.
  • the aliphatic sulfonyl group may be saturated or unsaturated, and is also a hydroxy group, an aromatic group, an aliphatic oxy group, a carbamoyl group, an aliphatic oxycarbonyl group, an aliphatic thio group, an amino group. It may have an aliphatic amino group, an acylamino group, a carbamoylamino group, or the like.
  • Examples of the aliphatic sulfonyl group include alkylsulfonyl groups having 1 to 6 total carbon atoms, preferably 1 to 4 total carbon atoms, such as methanesulfonyl.
  • the aromatic sulfonyl group has a hydroxy group, an aliphatic group, an aliphatic oxy group, a carbamoyl group, an aliphatic oxycarbonyl group, an aliphatic thio group, an amino group, an aliphatic amino group, an acylamino group, a carbamoylamino group and the like. You may have.
  • Examples of the aromatic sulfonyl group include arylsulfonyl groups having 6 to 10 carbon atoms in total, such as benzenesulfonyl.
  • the amino group may have an aliphatic group, an aromatic group, a heterocyclic group, or the like.
  • the acylamino group may have, for example, an acetylamino group, a benzoylamino group, a 2-pyridinecarbonylamino group, a propanoylamino group, or the like.
  • the above-mentioned acylamino group is an acylamino group having 2 to 12 total carbon atoms, preferably 2 to 8 carbon atoms in total, and more preferably an alkylcarbonylamino group having 2 to 8 carbon atoms in total, such as acetylamino group and benzoylamino group.
  • 2-pyridinecarbonylamino group, propanoylamino group and the like are examples of the alkylcarbonylamino group having 2 to 8 carbon atoms in total.
  • the aliphatic sulfonamide group, aromatic sulfonamide group, and heterocyclic sulfonamide group may be, for example, a methanesulfonamide group, a benzenesulfonamide group, a 2-pyridinesulfonamide group, or the like.
  • the sulfamoyl group may have an aliphatic group, an aromatic group, a heterocyclic group, or the like.
  • Examples of the sulfamoyl group include a sulfamoyl group, an alkylsulfamoyl group having a total of 1 to 9 carbon atoms, a dialkylsulfamoyl group having a total of 2 to 10 carbon atoms, and an arylsulfamoyl group having a total of 7 to 13 carbon atoms.
  • a heterocyclic sulfamoyl group having 2 to 12 carbon atoms more preferably a sulfamoyl group, an alkylsulfamoyl group having 1 to 7 carbon atoms, a dialkylsulfamoyl group having 3 to 6 carbon atoms, or a total carbon atom
  • the aliphatic oxy group may be saturated or unsaturated, and may have a methoxy group, an ethoxy group, an i-propyloxy group, a cyclohexyloxy group, a methoxyethoxy group, or the like.
  • Examples of the aliphatic oxy group include alkoxy groups having 1 to 8 carbon atoms, preferably 1 to 6 carbon atoms, such as methoxy group, ethoxy group, i-propyloxy group, cyclohexyloxy group and methoxyethoxy group.
  • the aromatic amino group and heterocyclic amino group are an aliphatic group, an aliphatic oxy group, a halogen atom, a carbamoyl group, a heterocyclic group condensed with the aryl group, an aliphatic oxycarbonyl group, preferably a total number of carbon atoms.
  • the aliphatic thio group may be saturated or unsaturated, and is an alkylthio group having 1 to 8 total carbon atoms, more preferably 1 to 6 total carbon atoms, such as methylthio group or ethylthio group. , Carbamoylmethylthio group, t-butylthio group and the like.
  • the carbamoylamino group may have an aliphatic group, an aryl group, a heterocyclic group, or the like.
  • Examples of the carbamoylamino group include a carbamoylamino group, an alkylcarbamoylamino group having 2 to 9 carbon atoms in total, a dialkylcarbamoylamino group having 3 to 10 carbon atoms in total, an arylcarbamoylamino group having 7 to 13 carbon atoms in total, Heterocyclic carbamoylamino group having 3 to 12 carbon atoms, preferably carbamoylamino group, alkylcarbamoylamino group having 2 to 7 carbon atoms, dialkylcarbamoylamino group having 3 to 6 carbon atoms, total carbon atom number 7 to 11 arylcarbamoylamino groups, heterocyclic carbamoylamino groups having 3 to 10 carbon atoms in total, such as carb
  • the range represented by the endpoints includes all numbers subsumed within that range (eg, 1-10 includes 1.4, 1.9, 2.33, 5.75, 9). .98 etc. are included).
  • reference to "at least 1" includes all numerical values equal to or greater than 1 (eg, at least 2, at least 4, at least 6, at least 8, at least 10, at least 25, at least 50, at least 100, etc.). ..
  • compositions of the present disclosure include polytetrafluoroethylene (hereinafter also referred to as "PTFE").
  • the PTFE usually has stretchability, fibrillating properties, and non-melt fabrication properties.
  • the above non-melting secondary processability means the property that the melt flow rate cannot be measured at a temperature higher than the crystallization melting point, that is, the property that it does not easily flow even in the melting temperature range, in accordance with ASTM D1238 and D2116.
  • the PTFE may be a tetrafluoroethylene (TFE) homopolymer or a modified PTFE obtained by copolymerizing TFE and a modifying monomer. From the viewpoint of stability and yield of the aqueous dispersion, the above PTFE is more preferably modified PTFE.
  • the modifying monomer is not particularly limited as long as it can be copolymerized with TFE, and examples thereof include a fluoromonomer and a non-fluoromonomer. Further, the modifying monomer to be used may be one kind or plural kinds.
  • non-fluoromonomer examples include methyl acrylate, methyl methacrylate, ethyl acrylate, ethyl methacrylate, propyl acrylate, propyl methacrylate butyl acrylate, butyl methacrylate, hexyl methacrylate, cyclohexyl methacrylate, vinyl methacrylate, vinyl acetate, acrylic acid, methacrylic acid, acrylonitrile. , Methacrylonitrile, ethyl vinyl ether, cyclohexyl vinyl ether and the like. Among them, butyl methacrylate, vinyl acetate and acrylic acid are preferable as the non-fluoromonomer.
  • fluoromonomers examples include perfluoroolefins such as hexafluoropropylene [HFP]; hydrogen-containing fluoroolefins such as trifluoroethylene and vinylidene fluoride [VDF]; perhaloolefins such as chlorotrifluoroethylene; perfluorovinyl ethers; Perfluoroalkyl) ethylene; perfluoroallyl ether and the like.
  • the “perfluoro organic group” means an organic group in which all hydrogen atoms bonded to carbon atoms are replaced with fluorine atoms.
  • the perfluoro organic group may have ether oxygen.
  • perfluorovinyl ether examples include perfluoro (alkyl vinyl ether) [PAVE] in which Rf is a perfluoroalkyl group having 1 to 10 carbon atoms in the general formula (A).
  • the carbon number of the perfluoroalkyl group is preferably 1-5.
  • Examples of the perfluoroalkyl group in PAVE include a perfluoromethyl group, a perfluoroethyl group, a perfluoropropyl group, a perfluorobutyl group, a perfluoropentyl group, and a perfluorohexyl group.
  • Examples of the above-mentioned perfluorovinyl ether further include those in which Rf is a perfluoro (alkoxyalkyl) group having 4 to 9 carbon atoms in the general formula (A), and Rf is the following formula:
  • Rf is a group represented by the following formula:
  • n an integer of 1 to 4
  • the (perfluoroalkyl) ethylene (PFAE) is not particularly limited, and examples thereof include (perfluorobutyl) ethylene (PFBE) and (perfluorohexyl) ethylene.
  • CF 2 CF-CF 2 -ORf (In the formula, Rf represents a perfluoro organic group.).
  • Rf in the general formula is the same as Rf in the general formula (A).
  • Rf a perfluoroalkyl group having 1 to 10 carbon atoms or a perfluoroalkoxyalkyl group having 1 to 10 carbon atoms is preferable.
  • a comonomer (3) having a monomer reactivity ratio of 0.1 to 8 is also preferably exemplified.
  • PTFE particles having a small average primary particle diameter and small aspect ratio can be obtained, and an aqueous dispersion having high dispersion stability can be obtained.
  • the monomer reactivity ratio in the copolymerization with TFE is the rate constant when the growing radical reacts with TFE when the growing radical is less than the repeating unit based on TFE, and the growing radical is a comonomer. It is the value divided by the rate constant when reacting. The lower this value, the higher the reactivity of the comonomer with TFE.
  • the monomer reactivity ratio can be calculated from the Feynman-Loss formula by copolymerizing TFE and a comonomer to determine the composition in the produced polymer immediately after the initiation.
  • the copolymerization was carried out by using 3600 g of deionized deaerated water, 1000 mass ppm of ammonium perfluorooctanoate and 100 g of paraffin wax in a stainless steel autoclave having an internal volume of 6.0 L under a pressure of 0. It is carried out at 78 MPaG and a temperature of 70 ° C. 0.05 g, 0.1 g, 0.2 g, 0.5 g, 1.0 g of comonomer was added to each reactor, 0.072 g of ammonium persulfate (20 mass ppm of water) was added, and the polymerization pressure was 0.78 MPaG. TFE is continuously supplied to maintain the temperature.
  • the stirring is stopped and the reactor is depressurized to atmospheric pressure. After cooling, the paraffin wax is separated to obtain an aqueous dispersion containing the produced polymer. The aqueous dispersion is stirred to coagulate the resulting polymer and dried at 150 ° C.
  • the composition in the obtained polymer is calculated by appropriately combining NMR, FT-IR, elemental analysis, and fluorescent X-ray analysis depending on the type of monomer.
  • the comonomer (3) having a monomer reactivity ratio of 0.1 to 8 is preferably at least one selected from the group consisting of comonomers represented by the formulas (3a) to (3d).
  • CH 2 CH-Rf 1 (3a) (In the formula, Rf 1 is a perfluoroalkyl group having 1 to 10 carbon atoms.)
  • CF 2 CF-O-Rf 2 (3b) (In the formula, Rf 2 is a perfluoroalkyl group having 1 to 2 carbon atoms.)
  • CF 2 CF-O- (CF 2 )
  • n CF CF 2 (3c) (In the formula, n is 1 or 2.)
  • X 3 and X 4 are F, Cl or a methoxy group, and Y is the formula Y1 or Y2.
  • the content of the comonomer (3) unit is preferably in the range of 0.00001 to 1.0 mass% with respect to the total polymerized units of PTFE.
  • 0.0001 mass% is more preferable, 0.0005 mass% is more preferable, 0.001 mass% is further preferable, and 0.005 mass% is further more preferable.
  • As the upper limit in order of preference, 0.90% by mass, 0.50% by mass, 0.40% by mass, 0.30% by mass, 0.20% by mass, 0.15% by mass, 0.10% by mass, 0 0.08% by mass, 0.05% by mass, and 0.01% by mass.
  • the average primary particle size is small, the aspect ratio of the primary particles is small, since it is possible to obtain an aqueous dispersion having excellent stability, hexafluoropropylene, chlorotrifluoroethylene, vinylidene fluoride, perfluoro At least one selected from the group consisting of (alkyl vinyl ether), (perfluoroalkyl) ethylene, ethylene, and a modified monomer having a functional group capable of reacting by radical polymerization and a hydrophilic group is preferable.
  • the modified monomer it is possible to obtain an aqueous dispersion of PTFE having a smaller average primary particle size, a smaller aspect ratio of primary particles, and excellent dispersion stability.
  • the modified monomer preferably contains at least one selected from the group consisting of hexafluoropropylene, perfluoro (alkyl vinyl ether) and (perfluoroalkyl) ethylene.
  • the modified monomer is more preferably from hexafluoropropylene, perfluoro (methyl vinyl ether), perfluoro (propyl vinyl ether), (perfluorobutyl) ethylene, (perfluorohexyl) ethylene, and (perfluorooctyl) ethylene.
  • the total amount of the above hexafluoropropylene unit, perfluoro (alkyl vinyl ether) unit and (perfluoroalkyl) ethylene unit is in the range of 0.00001 to 1.0 mass% with respect to the total polymerized units of PTFE.
  • the lower limit of the total amount is more preferably 0.0001% by mass, more preferably 0.0005% by mass, more preferably 0.001% by mass, further preferably 0.005% by mass, and 0.009% by mass. Particularly preferred.
  • modified monomer contains a modified monomer having a functional group capable of reacting by radical polymerization and a hydrophilic group (hereinafter referred to as “modified monomer (A)”).
  • modified monomer (A) a modified monomer having a functional group capable of reacting by radical polymerization and a hydrophilic group
  • modified monomer (A) makes it possible to obtain PTFE particles having a small primary particle diameter and an aqueous dispersion having high dispersion stability. Moreover, the aspect ratio of the primary particles can be reduced.
  • the amount of the modified monomer (A) used is preferably more than the amount corresponding to 0.1 mass ppm of the aqueous medium, more preferably more than 0.5 mass ppm, and 1.0 The amount is more preferably more than mass ppm, even more preferably 5 mass ppm or more, still more preferably 10 mass ppm or more. If the amount of the modified monomer (A) used is too small, the resulting PTFE may not have a small average primary particle size.
  • the amount of the modified monomer (A) used may be in the above range, but for example, the upper limit can be set to 5000 mass ppm. Further, in the above-mentioned production method, the modifying monomer (A) may be added to the system during the reaction in order to improve the stability of the aqueous dispersion during or after the reaction.
  • the modified monomer (A) Since the modified monomer (A) has high water solubility, even if the unreacted modified monomer (A) remains in the aqueous dispersion, it can be easily removed in the concentration step or the coagulation / washing step.
  • the above-mentioned modified monomer (A) is incorporated into the produced polymer during the polymerization process, but the concentration itself of the modified monomer (A) in the polymerization system is low and the amount incorporated into the polymer is small, so the heat resistance of PTFE decreases. There is no problem of coloring or coloring after firing.
  • Examples of the hydrophilic group in the modified monomer (A) include —NH 2 , —PO 3 M, —OPO 3 M, —SO 3 M, —OSO 3 M, and —COOM (M in each formula is H, Metal atom, NR 7y 4 , imidazolium which may have a substituent, pyridinium which may have a substituent or phosphonium which may have a substituent, R 7y is H or an organic group. Yes, they may be the same or different, and any two of them may be bonded to each other to form a ring).
  • As the hydrophilic group —SO 3 M or —COOM is preferable.
  • the organic group for R 7y is preferably an alkyl group.
  • R 7y is preferably an H or C 1-10 organic group, more preferably an H or C 1-4 organic group, and even more preferably an H or C 1-4 alkyl group.
  • the metal atom include monovalent and divalent metal atoms, alkali metal (group 1), alkaline earth metal (group 2), and the like, with Na, K, or Li being preferred.
  • Examples of the “functional group capable of reacting by radical polymerization” in the modified monomer (A) include groups having an ethylenically unsaturated bond such as vinyl group and allyl group.
  • the modified monomer (A) Since the modified monomer (A) has a functional group capable of reacting by radical polymerization, when used in the polymerization, it reacts with TFE in the early stage of the polymerization reaction and has a hydrophilic group derived from the modified monomer (A) and is stable. It is presumed that particles with high properties are formed. Therefore, it is considered that the number of particles increases when the polymerization is performed in the presence of the modified monomer (A).
  • one kind of the modified monomer (A) may be present, or two or more kinds thereof may be present.
  • a compound having an unsaturated bond can be used as the modifying monomer (A).
  • hydrophilic group examples include —NH 2 , —PO 3 M, —OPO 3 M, —SO 3 M, —OSO 3 M, and —COOM
  • M in each formula is H, a metal atom, NR 7y 4 , Imidazolium which may have a substituent, pyridinium which may have a substituent or phosphonium which may have a substituent
  • R 7y is H or an organic group, which may be the same or different. Any two of them may be bonded to each other to form a ring.
  • the organic group for R 7y is preferably an alkyl group.
  • R 7y is preferably an H or C 1-10 organic group, more preferably an H or C 1-4 organic group, and even more preferably an H or C 1-4 alkyl group.
  • the metal atom include monovalent and divalent metal atoms, alkali metal (group 1), alkaline earth metal (group 2), and the like, with Na, K, or Li being preferred.
  • linking group refers to a divalent linking group.
  • the linking group may be a single bond and preferably contains at least one carbon atom, and the number of carbon atoms may be 2 or more, 4 or more, and 8 or more. It may be 10 or more, or 20 or more. The upper limit is not limited, but may be, for example, 100 or less, and may be 50 or less.
  • the linking group may be linear or branched, cyclic or acyclic structure, saturated or unsaturated, substituted or unsubstituted, and optionally one or more selected from the group consisting of sulfur, oxygen, and nitrogen.
  • the linking group contains no carbon atoms and may be a catenary heteroatom such as oxygen, sulfur or nitrogen.
  • R a is preferably a catenary hetero atom such as oxygen, sulfur, or nitrogen, or a divalent organic group.
  • R a is a divalent organic group
  • the hydrogen atom bonded to the carbon atom may be replaced with a halogen other than fluorine, such as chlorine, and may or may not contain a double bond.
  • R a may be chain-like or branched, and may be cyclic or acyclic.
  • R a may also include a functional group (eg, ester, ether, ketone, amine, halide, etc.).
  • R a may also be a non-fluorine-containing divalent organic group or a partially fluorinated or perfluorinated divalent organic group.
  • R a is — (C ⁇ O) —, — (C ⁇ O) —O—, or a hydrocarbon group having 1 to 100 carbon atoms, which may contain an ether bond and may contain a carbonyl group. Is preferred, and in the hydrocarbon group, part or all of the hydrogen atoms bonded to carbon atoms may be replaced by fluorine.
  • R a is preferably — (CH 2 ) a —, — (CF 2 ) a —, —O— (CF 2 ) a —, — (CF 2 ) a —O— (CF 2 ) b —, —O.
  • a, b, c and d are independently at least 1 or more.
  • a, b, c and d may independently be 2 or more, 3 or more, 4 or more, 10 or more, 20 or more.
  • the upper limits of a, b, c and d are 100, for example.
  • Specific examples of the compound represented by the general formula (4) include: (In the formula, X j and Y 3 are the same as above. N is an integer of 1 to 10.) and the like.
  • X 7 are each independently H, F or CF 3
  • e is an integer of 0 to 3
  • g is 0 or 1
  • h is 0 or 1
  • i 0 or 1
  • Z 1 and Z 2 are each independently F or CF 3
  • a divalent group represented by the formula (t2) is also preferably a divalent group in which one of Z 1 and Z 2 is F. It is more preferable that the other is CF 3 .
  • the compound represented by the general formula (4) has a C—F bond and does not have a C—H bond except for the hydrophilic group (Y 3 ). That is, in the general formula (4), it is preferable that X i , X j , and X k are all F, and R a is a perfluoroalkylene group having 1 or more carbon atoms, and the above perfluoroalkylene group is , Chain-like or branched, cyclic or acyclic, and may contain at least one catenary heteroatom. The carbon number of the perfluoroalkylene group may be 2 to 20 or 4 to 18.
  • the compound represented by the general formula (4) may be partially fluorinated. That is, the compound represented by the general formula (4) has at least one hydrogen atom bonded to a carbon atom and at least one fluorine atom bonded to a carbon atom, except for the hydrophilic group (Y 3 ). Is also preferable.
  • the compound represented by the general formula (4) is also preferably a compound represented by the following formula (4a).
  • CF 2 CF-O-Rf 0 -Y 3 (4a)
  • Y 3 is a hydrophilic group
  • Rf 0 is perfluorinated, and may be a chain or branched, cyclic or acyclic structure, saturated or unsaturated, substituted or unsubstituted
  • a perfluorinated divalent linking group optionally containing one or more heteroatoms selected from the group consisting of sulfur, oxygen, and nitrogen.
  • the compound represented by the general formula (4) is also preferably a compound represented by the following formula (4b).
  • CH 2 CH-O-Rf 0 -Y 3 (4b)
  • Y 3 is a hydrophilic group
  • Rf 0 is a perfluorinated divalent linking group defined by the formula (4a).
  • Y 3 is —OSO 3 M.
  • M is the same
  • Y 3 is —COOM.
  • Y 3 is —OPO 3 M or —OP (O) (OM) 2 as one of the preferable forms.
  • Y 3 is —PO 3 M or —P (O) (OM) 2 as one of the preferable forms.
  • CX 2 CY (-Rf-Y 3 ) (7)
  • X is the same or different and is -H or -F
  • Y is -H, -F, an alkyl group or a fluorine-containing alkyl group
  • Rf is a fluorine-containing alkylene group having 1 to 40 carbon atoms.
  • a fluorine-containing alkylene group having an ether bond having 2 to 100 carbon atoms, Y 3 is the same as the above), and at least one selected from the group consisting of Preferably there is.
  • the above-mentioned fluorine-containing alkylene group having an ether bond having 2 to 100 carbon atoms is an alkylene group which does not include a structure in which an oxygen atom is a terminal and which contains an ether bond between carbon atoms.
  • X is -H or -F.
  • X may be both -F, or at least one may be -H.
  • one may be -F and the other may be -H, or both may be -H.
  • Y is —H, —F, an alkyl group or a fluorine-containing alkyl group.
  • the above-mentioned alkyl group is an alkyl group containing no fluorine atom and may have one or more carbon atoms.
  • the alkyl group preferably has 6 or less carbon atoms, more preferably 4 or less carbon atoms, and even more preferably 3 or less carbon atoms.
  • the above-mentioned fluorine-containing alkyl group is an alkyl group containing at least one fluorine atom, and may have one or more carbon atoms.
  • the fluorine-containing alkyl group preferably has 6 or less carbon atoms, more preferably 4 or less carbon atoms, and even more preferably 3 or less carbon atoms.
  • Y —H, —F or —CF 3 is preferable, and —F is more preferable.
  • Z is the same or different and is -H, -F, an alkyl group or a fluoroalkyl group.
  • the above-mentioned alkyl group is an alkyl group containing no fluorine atom and may have one or more carbon atoms.
  • the alkyl group preferably has 6 or less carbon atoms, more preferably 4 or less carbon atoms, and even more preferably 3 or less carbon atoms.
  • the above-mentioned fluorine-containing alkyl group is an alkyl group containing at least one fluorine atom, and may have one or more carbon atoms.
  • the fluorine-containing alkyl group preferably has 6 or less carbon atoms, more preferably 4 or less carbon atoms, and even more preferably 3 or less carbon atoms.
  • Z —H, —F or —CF 3 is preferable, and —F is more preferable.
  • X can be -H and Y and Z can be -F.
  • Rf is a fluorine-containing alkylene group having 1 to 40 carbon atoms or a fluorine-containing alkylene group having 2 to 100 carbon atoms and having an ether bond.
  • the fluorine-containing alkylene group preferably has 2 or more carbon atoms. Further, it is preferably 30 or less, more preferably 20 or less, still more preferably 10 or less.
  • fluorinated alkylene group -CF 2 -, - CH 2 CF 2 -, - CF 2 CF 2 -, - CF 2 CH 2 -, - CF 2 CF 2 CH 2 -, - CF (CF 3) - , -CF (CF 3) CF 2 -, - CF (CF 3) CH 2 - and the like.
  • the fluorine-containing alkylene group is preferably a perfluoroalkylene group.
  • the fluorine-containing alkylene group having an ether bond preferably has 3 or more carbon atoms. Further, the number of carbon atoms of the fluorine-containing alkylene group having an ether bond is preferably 60 or less, more preferably 30 or less, still more preferably 12 or less.
  • Examples of the fluorine-containing alkylene group having an ether bond include those represented by the following formula: (Wherein Z 1 is F or CF 3 ; Z 2 and Z 3 are each H or F; Z 4 is H, F or CF 3 ; p1 + q1 + r1 is an integer of 1 to 10; s1 is 0 or 1; t1 is 0 It is also preferably a divalent group represented by (integer of 5).
  • fluorine-containing alkylene group having an ether bond examples include —CF (CF 3 ) CF 2 —O—CF (CF 3 ) — and — (CF (CF 3 ) CF 2 —O) n —CF (CF 3 )-(in the formula, n is an integer of 1 to 10), -CF (CF 3 ) CF 2 -O-CF (CF 3 ) CH 2 -,-(CF (CF 3 ) CF 2 -O) n- CF (CF 3 ) CH 2 — (where n is an integer of 1 to 10), —CH 2 CF 2 CF 2 O—CH 2 CF 2 CH 2 —, —CF 2 CF 2 CF 2 O—CF 2 CF 2- , —CF 2 CF 2 CF 2 O—CF 2 CF 2 CH 2 —, —CF 2 CF 2 O—CF 2 —, —CF 2 CF 2 O—CF 2 CH 2 — and the like can be mentioned.
  • Y 3 is —COOM, —SO 3 M or —OSO 3 M
  • M is H, a metal atom, NR 7y 4 , an imidazolium which may have a substituent, a substituent R7y is pyridinium which may have or phosphonium which may have a substituent, R 7y is H or an organic group, and may be the same or different. May be formed).
  • the organic group for R 7y is preferably an alkyl group.
  • R 7y is preferably an H or C 1-10 organic group, more preferably an H or C 1-4 organic group, and even more preferably an H or C 1-4 alkyl group.
  • the metal atom examples include an alkali metal (group 1) and an alkaline earth metal (group 2), and Na, K or Li is preferable.
  • M —H, a metal atom or —NR 7y 4 is preferable, —H, an alkali metal (Group 1), an alkaline earth metal (Group 2) or —NR 7y 4 is more preferable, —H, —Na , -K, -Li or -NH 4 are more preferable, -Na, preferably from -K or -NH 4 further particularly preferred -Na or -NH 4, -NH 4 is most preferred.
  • Y 3 , -COOM or -SO 3 M is preferable, and -COOM is more preferable.
  • the monomer represented by the general formula (5) is preferably the monomer (5a) represented by the general formula (5a).
  • CH 2 CF (-CF 2 -O-Rf-Y 3 ) (5a) (In the formula, Rf and Y 3 are the same as above.)
  • Z 1 is F or CF 3 ; Z 2 and Z 3 are H or F, respectively; Z 4 is H, F or CF 3 ; p1 + q1 + r1 is an integer of 0 to 10; s1 is 0 or 1, and t1 is 0. An integer of 5 to 5, Y 3 is the same as above, provided that when Z 3 and Z 4 are both H, a monomer represented by p1 + q1 + r1 + s1 is not 0). More specifically,
  • the monomer represented by the general formula (5) is preferably the monomer (5b) represented by the general formula (5b).
  • CX 2 2 CFCF 2 —O— (CF (CF 3 ) CF 2 O) n5 —CF (CF 3 ) —Y 3 (5b)
  • each X 2 is the same and represents F or H.
  • n5 represents 0 or an integer of 1 to 10, and
  • Y 3 is the same as the above definition.
  • n5 is preferably 0 or an integer of 1 to 5, more preferably 0, 1 or 2, from the viewpoint that PTFE particles having a small primary particle size can be obtained. It is more preferably 0 or 1.
  • the above Y 3 is preferably —COOM from the viewpoint of obtaining appropriate water solubility and surface activity, and the above M is less likely to remain as an impurity, so that the obtained composition and a stretched product obtained from the composition can be obtained. From the viewpoint of improving heat resistance, H or NH 4 is preferable.
  • the polymer (5) may be a homopolymer of the fluoroallyl ether compound represented by the general formula (5b) or a copolymer with another monomer.
  • Examples of the perfluorovinylalkyl compound represented by the above formula (5b) include CH 2 ⁇ CFCF 2 OCF (CF 3 ) COOM, CH 2 ⁇ CFCF 2 OCF (CF 3 ) CF 2 OCF (CF 3 ) COOM ( In the formula, M is the same as the above definition).
  • examples of the monomer represented by the general formula (5) include a monomer represented by the general formula (5c).
  • CF 2 CFCF 2 -O-Rf-Y 3 (5c) (In the formula, Rf and Y 3 are the same as above)
  • X is —H or —F.
  • X may be both -F, or at least one may be -H.
  • one may be -F and the other may be -H, or both may be -H.
  • Y is —H, —F, an alkyl group or a fluorine-containing alkyl group.
  • the above-mentioned alkyl group is an alkyl group containing no fluorine atom and may have one or more carbon atoms.
  • the alkyl group preferably has 6 or less carbon atoms, more preferably 4 or less carbon atoms, and even more preferably 3 or less carbon atoms.
  • the above-mentioned fluorine-containing alkyl group is an alkyl group containing at least one fluorine atom, and may have one or more carbon atoms.
  • the fluorine-containing alkyl group preferably has 6 or less carbon atoms, more preferably 4 or less carbon atoms, and even more preferably 3 or less carbon atoms.
  • Y —H, —F or —CF 3 is preferable, and —F is more preferable.
  • X and Y contains a fluorine atom.
  • X can be -H and Y and Z can be -F.
  • Rf is a fluorine-containing alkylene group having 1 to 40 carbon atoms or a fluorine-containing alkylene group having 2 to 100 carbon atoms and having an ether bond.
  • the fluorine-containing alkylene group preferably has 2 or more carbon atoms. Further, the number of carbon atoms of the fluorine-containing alkylene group is preferably 30 or less, more preferably 20 or less, still more preferably 10 or less.
  • fluorinated alkylene group -CF 2 -, - CH 2 CF 2 -, - CF 2 CF 2 -, - CF 2 CH 2 -, - CF 2 CF 2 CH 2 -, - CF (CF 3) - , -CF (CF 3) CF 2 -, - CF (CF 3) CH 2 - and the like.
  • the fluorine-containing alkylene group is preferably a perfluoroalkylene group.
  • the monomer represented by the general formula (6) is at least selected from the group consisting of monomers represented by the general formulas (6a), (6b), (6c), (6d) and (6e).
  • One kind is preferable.
  • CF 2 CF-O- (CF 2 ) n1- Y 3 (6a)
  • n1 represents an integer of 1 to 10
  • Y 3 represents —COOM, —SO 3 M or —OSO 3 M
  • M is H, a metal atom, NR 7y 4 or has a substituent.
  • imidazolium, optionally substituted pyridinium or optionally substituted phosphonium, R 7y is H or an organic group, which may be the same or different.
  • n1 is preferably an integer of 5 or less, and more preferably an integer of 2 or less.
  • the above Y 3 is preferably —COOM from the viewpoint of obtaining appropriate water solubility and stability of the aqueous dispersion, and M is less likely to remain as an impurity and the heat resistance of the obtained molded body is improved.
  • H or NH 4 is preferred.
  • Examples of the monomer represented by the above formula (6a) include CF 2 ⁇ CF—O—CF 2 COOM, CF 2 ⁇ CF (OCF 2 CF 2 COOM), and CF 2 ⁇ CF (OCF 2 CF 2 CF). 2 COOM) (wherein M is as defined above).
  • n2 is preferably an integer of 3 or less from the viewpoint of stability of the obtained aqueous dispersion
  • Y 3 is an appropriate water solubility and stability of the aqueous dispersion.
  • —COOM is preferable
  • M is preferably H or NH 4 because it hardly remains as an impurity and the heat resistance of the obtained molded body is improved.
  • n3 is preferably 5 or less integer in terms of water-soluble
  • the Y 3 is in that the stability of the proper water solubility and an aqueous dispersion is obtained
  • -COOM Is preferable and M is preferably H or NH 4 in terms of improving dispersion stability.
  • X 1 is preferably —CF 3 in terms of stability of the aqueous dispersion
  • n 4 is preferably an integer of 5 or less in terms of water solubility
  • the Y 3 is preferably —COOM from the viewpoint of obtaining appropriate water solubility and stability of the aqueous dispersion
  • the M is preferably H or NH 4 .
  • n5 is preferably 5 or less integer in terms of water-soluble
  • the Y 3 is a -COOM in that the stability of the proper water solubility and an aqueous dispersion is obtained
  • M is H or NH 4 .
  • Examples of the monomer represented by the general formula (6e) include CF 2 ⁇ CFOCF 2 CF 2 CF 2 COOM (wherein M represents H, NH 4 or an alkali metal).
  • Rf is preferably a fluorine-containing alkylene group having 1 to 40 carbon atoms.
  • at least one of X and Y preferably contains a fluorine atom.
  • the above Y 3 is preferably —SO 3 M or —COOM, and M is H, a metal atom, NR 7y 4 , an imidazolium which may have a substituent, a pyridinium which may have a substituent, or It is preferably phosphonium which may have a substituent.
  • R 7y represents H or an organic group. Examples of the metal atom include monovalent and divalent metal atoms, alkali metal (group 1), alkaline earth metal (group 2), and the like, with Na, K, or Li being preferred.
  • n1 is preferably an integer of 5 or less, more preferably an integer of 2 or less.
  • the above Y 3 is preferably —COOM from the viewpoint of obtaining appropriate water solubility and surface activity, and M is less likely to remain as an impurity, and the heat resistance of the obtained composition and the stretched body obtained from the composition are high. From the viewpoint of improving the property, H or NH 4 is preferable.
  • Examples of the perfluorovinylalkyl compound represented by the above formula (7a) include CF 2 ⁇ CFCF 2 COOM (wherein M is as defined above).
  • n2 is preferably an integer of 3 or less from the viewpoint that PTFE particles having a small primary particle size can be obtained, and Y 3 is a water-soluble compound and has a suitable surface activity.
  • —COOM is preferable, and M is H or NH 4 in that it hardly remains as an impurity and the heat resistance of the composition obtained and the stretched body obtained from the composition is improved. preferable.
  • the modified monomer preferably contains the modified monomer (A), and is represented by the general formula (5a), the general formula (5c), the general formula (6a), the general formula (6b), the general formula (6c), and the general formula (6c). It preferably contains at least one selected from the group consisting of compounds represented by formula (6d), and more preferably contains a compound represented by formula (5a) or formula (5c).
  • the content of the modifying monomer (A) unit is preferably in the range of 0.00001 to 1.0 mass% with respect to the total polymerized units of PTFE.
  • the lower limit is more preferably 0.0001% by mass, further preferably 0.0005% by mass, still more preferably 0.001% by mass, and particularly preferably 0.005% by mass.
  • As the upper limit in order of preference, 0.90% by mass, 0.50% by mass, 0.40% by mass, 0.30% by mass, 0.20% by mass, 0.15% by mass, 0.10% by mass, 0 0.08% by mass, 0.05% by mass, and 0.01% by mass.
  • each monomer unit constituting PTFE can be calculated by appropriately combining NMR, FT-IR, elemental analysis, and fluorescent X-ray analysis depending on the type of monomer.
  • the content of each monomer unit constituting PTFE can also be calculated from the addition amount of the modified monomer used in the polymerization.
  • the aspect ratio of primary particles is preferably less than 2.00, more preferably 1.90 or less, still more preferably 1.80 or less, still more preferably 1.70 or less, particularly preferably 1.60 or less. , 1.50 or less are particularly preferable.
  • the aspect ratio is more preferably 1.45 or less, still more preferably 1.40 or less, even more preferably 1.35 or less, particularly preferably 1.30 or less, particularly preferably 1.20 or less, 1.10
  • the following are the most preferable.
  • the above-mentioned aspect ratio was obtained by observing a PTFE aqueous dispersion diluted with a solid content concentration of about 1 mass% with a scanning electron microscope (SEM) and randomly extracting 400 pieces.
  • SEM scanning electron microscope
  • Image processing is performed on the above particles, and the average is calculated from the ratio of the major axis and the minor axis.
  • the above-mentioned aspect ratio can be obtained by irradiating the PTFE powder with an electron beam, adding it to an aqueous solution of a fluorosurfactant, and redispersing it with ultrasonic waves to obtain an aqueous PTFE dispersion. .
  • the aspect ratio is determined from this PTFE aqueous dispersion by the same method as the method of measuring with the above aqueous dispersion.
  • a PTFE aqueous dispersion prepared so that the polymer solid content concentration is about 1.0 mass% is prepared, and a scanning electron microscope ( By observing with SEM), image processing is performed on 400 or more particles randomly extracted, and the aspect ratio can be determined from the average of the ratio of the major axis and the minor axis.
  • a scanning electron microscope By observing with SEM
  • image processing is performed on 400 or more particles randomly extracted, and the aspect ratio can be determined from the average of the ratio of the major axis and the minor axis.
  • the PTFE preferably has an endothermic peak temperature in the range of 333 to 347 ° C. More preferably, it is 335 ° C. or higher and 345 ° C. or lower.
  • the above endothermic peak temperature corresponds to the maximum value in the heat of fusion curve when PTFE having no history of being heated to a temperature of 300 ° C. or higher is heated at a rate of 10 ° C./min using a differential scanning calorimeter [DSC]. Is the temperature.
  • PTFE For the endothermic peak temperature of PTFE, about 10 mg of PTFE powder with no history of heating to a temperature of 300 ° C or higher is precisely weighed and stored in a dedicated aluminum pan, and TG / DTA (differential thermogravimetric simultaneous measurement device) is used. Can be used to measure.
  • the endothermic peak temperature was obtained by obtaining a differential heat (DTA) curve by raising the temperature of the aluminum pan in the air atmosphere in the temperature range from 25 ° C. to 600 ° C. under the condition of 10 ° C./min. It can be specified as the temperature corresponding to the maximum value in the DTA) curve.
  • DTA differential heat
  • the above-mentioned PTFE is preferably PTFE which has no history of being heated at a temperature equal to or higher than the primary endothermic peak temperature.
  • the PTFE may be unsintered PTFE or semi-sintered PTFE. From the viewpoint of a simple process or the ease of controlling the thickness and pore size, unsintered PTFE is preferable.
  • semi-baked PTFE is preferable from the viewpoint of increasing the strength of the biaxially stretched film or reducing the pore size.
  • unsintered PTFE include PTFE after polymerization.
  • the unsintered PTFE is PTFE that has no history of being heated to a temperature of the secondary endothermic peak temperature or higher
  • the semi-sintered PTFE is PTFE that has no history of being heated to a temperature of the primary endothermic peak temperature or higher.
  • the PTFE is heated at a temperature not higher than the primary endothermic peak temperature and not lower than the secondary endothermic peak temperature.
  • the primary endothermic peak temperature means the maximum peak temperature of the endothermic curve that appears on the crystal melting curve when unsintered PTFE is measured by a differential scanning calorimeter.
  • the secondary endothermic peak temperature means the maximum peak temperature of the endothermic curve appearing on the crystal melting curve when PTFE heated to a temperature equal to or higher than the primary endothermic peak temperature (for example, 360 ° C.) is measured by a differential scanning calorimeter. To do.
  • the above-mentioned endothermic curve is obtained by using a differential scanning calorimeter to raise the temperature at a temperature rising rate of 10 ° C./min.
  • the PTFE may have a core-shell structure.
  • the core-shell structure is a conventionally known structure and is a structure of primary particles in an aqueous dispersion which can be produced by the method described in US Pat. No. 6,841,594.
  • Examples of the PTFE having a core-shell structure include, for example, a core-shell structure including a core portion of TFE homopolymer and a shell portion of modified PTFE, a core-shell structure including a core portion of modified PTFE and a shell portion of TFE homopolymer, and modified PTFE. And a shell portion of a modified PTFE having a monomer composition different from that of the modified PTFE forming the core portion.
  • the PTFE having the above core-shell structure is prepared, for example, by first polymerizing TFE and optionally a modified monomer to produce a core part (TFE homopolymer or modified PTFE), and then polymerizing TFE and optionally a modified monomer.
  • TFE homopolymer or modified PTFE can be obtained by producing a shell part (TFE homopolymer or modified PTFE).
  • the shell part means a part forming a predetermined thickness from the surface of the PTFE primary particles to the inside of the particle, and the core part means a part forming the inside of the shell part.
  • the core portion and the shell portion have different monomer compositions
  • the core portion and the shell portion have the same monomer composition
  • All of those having different number average molecular weights and (3) having different monomer compositions in the core portion and the shell portion and having different number average molecular weights in both portions are also included.
  • the content of the modifying monomer in the shell part is preferably 0.0001 to 1% by mass. It is more preferably 0.001% by mass or more, and further preferably 0.01% by mass or more. Further, it is more preferably 0.50 mass% or less, and further preferably 0.30 mass% or less.
  • the content of the modifying monomer in the core portion is preferably 0.00001 to 1.0% by mass. It is more preferably 0.0001% by mass or more, and further preferably 0.001% by mass or more. Further, it is more preferably 0.50 mass% or less, and further preferably 0.30 mass% or less.
  • the average primary particle diameter of the primary particles is preferably 500 nm or less, more preferably 400 nm or less, and further preferably 350 nm or less. Since the average primary particle diameter of the primary particles is relatively small, the polymerization of TFE in an aqueous medium proceeds smoothly, and PTFE can be easily produced.
  • the relatively small average primary particle diameter of the primary particles can be obtained, for example, by adding the modifying monomer to the polymerization system at the initial stage of the TFE polymerization.
  • the lower limit of the average primary particle size is not particularly limited, but may be 50 nm or 100 nm, for example. From the viewpoint of the molecular weight, it is preferably 100 nm or more, and more preferably 150 nm or more.
  • the average primary particle diameter of the primary particles of PTFE can be measured by the dynamic light scattering method.
  • a PTFE aqueous dispersion in which the polymer solid content concentration was adjusted to about 1.0 mass% was prepared, and the measurement temperature was 25 ° C. and the refractive index of the solvent (water) was 1. using the dynamic light scattering method. 3328, the viscosity of the solvent (water) is 0.8878 mPa ⁇ s, and the number of times of integration is 70.
  • ELSZ-1000S manufactured by Otsuka Electronics Co., Ltd.
  • the PTFE may have a thermal instability index (TII) of 20 or more.
  • the thermal instability index (TII) of PTFE can be adjusted within the above range, for example, by producing PTFE using the polymer (I).
  • TII is preferably 25 or more, more preferably 30 or more, and further preferably 35 or more. It is particularly preferably 40 or more.
  • the TII is measured according to ASTM D 4895-89.
  • the 0.1% mass reduction temperature of PTFE may be 400 ° C. or lower.
  • the 0.1% mass reduction temperature of PTFE can be adjusted within the above range, for example, by producing PTFE using the polymer (I).
  • 0.1% mass reduction temperature about 10 mg of PTFE powder that has no history of being heated to a temperature of 300 ° C. or higher is precisely weighed and stored in a dedicated aluminum pan, and TG / DTA (differential thermogravimetric simultaneous measurement device ) Can be used for measurement.
  • the 0.1% mass reduction temperature corresponds to the point that the mass is decreased by 0.1% by mass by raising the temperature of the aluminum pan in the atmosphere from 25 ° C to 600 ° C under the condition of 10 ° C / min. It can be specified as the temperature.
  • the 1.0% weight loss temperature of PTFE may be 492 ° C or lower.
  • the 1.0% mass reduction temperature of PTFE can be adjusted within the above range, for example, by producing PTFE using the polymer (I).
  • 1.0% mass reduction temperature about 10 mg of PTFE powder with no history of heating to a temperature of 300 ° C or higher is precisely weighed and stored in a dedicated aluminum pan, and TG / DTA (differential thermogravimetric simultaneous measurement device ) Can be used for measurement.
  • the 1.0% mass reduction temperature corresponds to a point in which the mass of the aluminum pan is reduced by 1.0 mass% by raising the temperature of the aluminum pan in the temperature range from 25 ° C to 600 ° C under the condition of 10 ° C / min. It can be specified as the temperature.
  • the composition of the present disclosure comprises a polymer (I) containing a polymerized unit (I) based on a monomer represented by the general formula (I).
  • the polymer (I) preferably contains two or more polymerized units (I).
  • CX 1 X 3 CX 2 R (-CZ 1 Z 2 -A 0 ) m (I) (In the formula, X 1 and X 3 are each independently F, Cl, H or CF 3 ; A 0 is an anionic group; X 2 is H, F, an alkyl group or a fluorine-containing group.
  • R is a linking group; Z 1 and Z 2 are each independently H, F, an alkyl group or a fluorine-containing alkyl group; m is an integer of 1 or more.) As X 2 , F, Cl, H or CF 3 is preferable. Further, as Z 1 and Z 2 , F or CF 3 is preferable.
  • the anionic group is a functional group which provides an anionic group such as a sulfate group or a carboxylate group, an acid group such as —COOH, and an acid group such as —COONH 4. Is included.
  • the anionic group is a sulfate group, a carboxylate group, a phosphate group, a phosphonate group, a sulfonate group, or —C (CF 3 ) 2 OM (wherein M is —H, a metal atom, —NR 7 4 , It is imidazolium which may have a substituent, pyridinium which may have a substituent or phosphonium which may have a substituent, and R 7 is H or an organic group.) Is preferable. A sulfate group, a carboxylate group, a phosphate group, a phosphonate group or a sulfonate group is more preferable.
  • the polymer (I) may contain only the polymerized unit (I) based on one kind of monomer represented by the general formula (I), or may be represented by the general formula (I): It may contain polymerized units (I) based on one or more types of monomers.
  • R is a linking group.
  • the “linking group” is a (m + 1) -valent linking group, and when m is 1, it is a divalent linking group.
  • the linking group may be a single bond and preferably contains at least one carbon atom, and the number of carbon atoms may be 2 or more, 4 or more, and 8 or more. It may be 10 or more, or 20 or more.
  • the upper limit is not limited, but may be, for example, 100 or less, and may be 50 or less.
  • the linking group may be linear or branched, cyclic or acyclic structure, saturated or unsaturated, substituted or unsubstituted, and optionally one or more selected from the group consisting of sulfur, oxygen, and nitrogen. It may contain heteroatoms and optionally one or more functional groups selected from the group consisting of esters, amides, sulfonamides, carbonyls, carbonates, urethanes, ureas and carbamates.
  • the linking group does not contain a carbon atom and may be a catenary heteroatom such as oxygen, sulfur or nitrogen.
  • n is an integer of 1 or more, preferably 1 or 2, and more preferably 1.
  • Z 1 , Z 2 and A 0 may be the same or different.
  • R is preferably, for example, a catenary hetero atom such as oxygen, sulfur, or nitrogen, or a divalent organic group.
  • R When R is a divalent organic group, the hydrogen atom bonded to the carbon atom may be replaced with a halogen other than fluorine, such as chlorine, and may or may not contain a double bond.
  • R may be chain-like or branched, and may be cyclic or acyclic.
  • R may also include a functional group (eg, ester, ether, ketone, amine, halide, etc.).
  • R may also be a non-fluorine-containing divalent organic group or a partially fluorinated or perfluorinated divalent organic group.
  • a hydrocarbon group in which a fluorine atom is not bonded to a carbon atom a hydrocarbon group in which a part of hydrogen atoms bonded to a carbon atom are substituted with a fluorine atom, or a hydrogen atom bonded to a carbon atom May all be a hydrocarbon group substituted with a fluorine atom, and these may contain an oxygen atom, a double bond or a functional group.
  • R is preferably a hydrocarbon group having 1 to 100 carbon atoms which may contain an ether bond, and in the hydrocarbon group, some or all of hydrogen atoms bonded to carbon atoms are substituted with fluorine. May be.
  • R is preferably — (CH 2 ) a —, — (CF 2 ) a —, —O— (CF 2 ) a —, — (CF 2 ) a —O— (CF 2 ) b —, —O ( CF 2 ) a- O- (CF 2 ) b -,-(CF 2 ) a- [O- (CF 2 ) b ] c- , -O (CF 2 ) a- [O- (CF 2 ) b ] c , —O (CF 2 ) a- [O- (CF 2 ) b ] c ⁇ , — [(CF 2 ) a —O] b — [(CF 2 ) c —O] d —, —O [(CF 2 ) a —O] b — [(CF 2 ) c —O] d -, —O [(CF 2 ) a —
  • a, b, c and d are independently at least 1 or more.
  • a, b, c and d may independently be 2 or more, 3 or more, 4 or more, 10 or more, 20 or more.
  • the upper limits of a, b, c and d are 100, for example.
  • R is the following general formula (r1): --CF 2 --O-(CX 6 2 ) e- ⁇ O--CF (CF 3 ) ⁇ f- (O) g- (r1) (Wherein, X 6 is independently H, F or CF 3 , e is an integer of 0 to 3, f is an integer of 0 to 3, and g is 0 or 1) Is preferably a divalent group represented by the following general formula (r2): --CF 2 --O-(CX 7 2 ) e- (O) g- (r2) (In the formula, X 7 is each independently H, F or CF 3 , e is an integer of 0 to 3, and g is 0 or 1).
  • R is preferably a perfluoroalkylene group which may contain an oxygen atom, and specifically, —CF 2 —O—, —CF 2 —O—CF 2 —, —CF 2 —O—CF 2 CF 2 -, - CF 2 -O -CF (CF 3) -, - CF 2 -O-CF (CF 3) CF 2 -, or, -CF 2 -O-CF (CF 3) CF 2 -O- Is preferred.
  • -R-CZ 1 Z 2 - is represented by the following formula (s2): --CF 2 --O-(CX 7 2 ) e- (O) g --CZ 1 Z 2- (s2)
  • X 7 are each independently H, F or CF 3
  • e is an integer of 0 to 3
  • g is 0 or 1
  • Z 1 and Z 2 are each independently H, F, an alkyl group or a fluorine-containing alkyl group
  • Z 1 and Z 2 are more preferably F or CF 3 , and one is F. More preferably, the other is CF 3 .
  • Examples of —R—CZ 1 Z 2 — of the general formula (I) include —CF 2 —O—CF 2 —, —CF 2 —O—CF (CF 3 ) —, and —CF 2 —O—C (CF 3).
  • polymer (I) is highly fluorinated.
  • anionic groups (A 0 ) such as phosphate group moieties (eg CH 2 OP (O) (OM) 2 ) and sulfate group moieties (eg CH 2 OS (O) 2 OM)
  • polymers It is preferable that 80% or more, 90% or more, 95% or more, or 100% of the C—H bond in (I) is substituted with a C—F bond.
  • the polymer (I) has a C—F bond and does not have a C—H bond, except for the anionic group (A 0 ). That is, in the general formula (I), all of X 1 , X 2 , and X 3 are F, R is preferably a perfluoroalkylene group having 1 or more carbon atoms, and the above perfluoroalkylene group is It may be chain-like or branched-chain, cyclic or acyclic, and may contain at least one catenary heteroatom. The carbon number of the perfluoroalkylene group may be 2 to 20 or 4 to 18.
  • the polymer (I) may be partially fluorinated. That is, the polymer (I) preferably has at least one hydrogen atom bonded to a carbon atom and at least one fluorine atom bonded to a carbon atom, except for the anionic group (A 0 ).
  • the anionic group (A 0 ) includes —SO 3 M, —OSO 3 M, —COOM, —SO 2 NR′CH 2 COOM, —CH 2 OP (O) (OM) 2 , [—CH 2 O] 2 P (O) (OM), -CH 2 CH 2 OP (O) (OM) 2 , [-CH 2 CH 2 O] 2 P (O) (OM), -CH 2 CH 2 OSO 3 M, -P (O) (OM) 2 , —SO 2 NR′CH 2 CH 2 OP (O) (OM) 2 , [—SO 2 NR′CH 2 CH 2 O] 2 P (O) (OM), —CH 2 It may be OSO 3 M, —SO 2 NR′CH 2 CH 2 OSO 3 M, or —C (CF 3 ) 2 OM. Among them, -SO 3 M, -COOM or -P (O) (OM) 2 is preferable, -SO 3 M or -COOM is more preferable,
  • M is H, a metal atom, NR 7 4 , imidazolium which may have a substituent, pyridinium which may have a substituent or phosphonium which may have a substituent, and R 7 Is H or an organic group.
  • metal atom examples include alkali metals (group 1) and alkaline earth metals (group 2), with Na, K or Li being preferred.
  • —H a metal atom or —NR 7 4 is preferable, —H, an alkali metal (Group 1), an alkaline earth metal (Group 2) or —NR 7 4 is more preferable, —H, —Na, -K, -Li or -NH 4 are more preferable, -Na, preferably from -K or -NH 4 further particularly preferred -Na or -NH 4, -NH 4 is most preferred.
  • each polymerized unit (I) may have different anionic groups or the same anionic group.
  • the polymer (I) is also preferably a polymer containing a polymerized unit (Ia) based on a monomer represented by the following formula (Ia).
  • CF 2 CF-O-Rf 0 -A 0 (Ia)
  • a 0 is an anionic group
  • Rf 0 is perfluorinated, and is linear or branched, cyclic or acyclic structure, saturated or unsaturated, substituted or unsubstituted Often, it is a perfluorinated divalent linking group optionally containing one or more heteroatoms selected from the group consisting of sulfur, oxygen, and nitrogen.
  • the above polymer (I) is also preferably a polymer containing a polymerized unit (Ib) based on a monomer represented by the following formula (Ib).
  • CH 2 CH-O-Rf 0 -A 0 (Ib)
  • a 0 is an anionic group
  • Rf 0 is a perfluorinated divalent linking group defined by the formula (Ia).
  • a 0 is a sulfate group.
  • a 0 is, for example, —CH 2 OSO 3 M, —CH 2 CH 2 OSO 3 M, or —SO 2 NR′CH 2 CH 2 OSO 3 M, where R ′ is H or the number of carbon atoms. It is an alkyl group of 1 to 4, and M is the same as above.
  • a 0 is a sulfonate group.
  • a 0 is, for example, —SO 3 M, and in the formula, M is the same as above.
  • a 0 is a sulfonate group
  • M is the same as above.
  • a 0 is a carboxylate group.
  • a 0 is, for example, COOM or SO 2 NR′CH 2 COOM, in which R ′ is H or an alkyl group having 1 to 4 carbon atoms, and M is the same as above.
  • the monomer represented by the general formula (I) includes CF 2 ⁇ CF (OCF 2 CF 2 COOM) and CF 2 ⁇ CF (O (CF 2 ) 3 COOM).
  • a 0 is a phosphate group.
  • a 0 for example, —CH 2 OP (O) (OM) 2 , [—CH 2 O] 2 P (O) (OM), —CH 2 CH 2 OP (O) (OM) 2 , [ ⁇ CH 2 CH 2 O] 2 P (O) (OM), [—SO 2 NR′CH 2 CH 2 O] 2 P (O) (OM) or —SO 2 NR′CH 2 CH 2 OP (O) ( OM) 2 , wherein R ′ is an alkyl group having 1 to 4 carbon atoms, and M is the same as above.
  • a 0 is a phosphonate group.
  • the polymer (I) is preferably a polymer (1) containing a polymer unit (1) based on a monomer represented by the following general formula (1).
  • CX 2 CY (-CZ 2 -O-Rf-A) (1)
  • X is the same or different and is -H or -F
  • Y is -H, -F
  • Z is the same or different, -H, -F.
  • Rf is a fluorine-containing alkylene group having 1 to 40 carbon atoms, or a fluorine-containing alkylene group having an ether bond having 2 to 100 carbon atoms
  • A is —COOM, — SO 3 M, —OSO 3 M or C (CF 3 ) 2 OM
  • M is —H, a metal atom, —NR 7 4 , imidazolium which may have a substituent, or a substituent Is pyridinium or optionally substituted phosphonium
  • R 7 is H or an organic group, provided that at least one of X, Y and Z contains a fluorine atom.
  • the above-mentioned fluorine-containing alkylene group having an ether bond having 2 to 100 carbon atoms is an alkylene group having no ether atom-terminated structure and having an ether bond between carbon atoms.
  • X is —H or —F.
  • X may be both -F, or at least one may be -H.
  • one may be -F and the other may be -H, or both may be -H.
  • Y is —H, —F, an alkyl group or a fluorine-containing alkyl group.
  • the above-mentioned alkyl group is an alkyl group containing no fluorine atom and may have one or more carbon atoms.
  • the alkyl group preferably has 6 or less carbon atoms, more preferably 4 or less carbon atoms, and even more preferably 3 or less carbon atoms.
  • the above-mentioned fluorine-containing alkyl group is an alkyl group containing at least one fluorine atom, and may have one or more carbon atoms.
  • the fluorine-containing alkyl group preferably has 6 or less carbon atoms, more preferably 4 or less carbon atoms, and even more preferably 3 or less carbon atoms.
  • Y —H, —F or —CF 3 is preferable, and —F is more preferable.
  • Z is the same or different and is -H, -F, an alkyl group or a fluoroalkyl group.
  • the above-mentioned alkyl group is an alkyl group containing no fluorine atom and may have one or more carbon atoms.
  • the alkyl group preferably has 6 or less carbon atoms, more preferably 4 or less carbon atoms, and even more preferably 3 or less carbon atoms.
  • the above-mentioned fluorine-containing alkyl group is an alkyl group containing at least one fluorine atom, and may have one or more carbon atoms.
  • the fluorine-containing alkyl group preferably has 6 or less carbon atoms, more preferably 4 or less carbon atoms, and even more preferably 3 or less carbon atoms.
  • Z —H, —F or —CF 3 is preferable, and —F is more preferable.
  • At least one of X, Y and Z contains a fluorine atom.
  • X can be -H and Y and Z can be -F.
  • Rf is a fluorine-containing alkylene group having 1 to 40 carbon atoms or a fluorine-containing alkylene group having 2 to 100 carbon atoms and having an ether bond.
  • the fluorine-containing alkylene group preferably has 2 or more carbon atoms.
  • the number of carbon atoms in the fluorine-containing alkylene group is preferably 30 or less, more preferably 20 or less, still more preferably 10 or less.
  • fluorinated alkylene group -CF 2 -, - CH 2 CF 2 -, - CF 2 CF 2 -, - CF 2 CH 2 -, - CF 2 CF 2 CH 2 -, - CF (CF 3) - , -CF (CF 3) CF 2 -, - CF (CF 3) CH 2 - and the like.
  • the fluorine-containing alkylene group is preferably a perfluoroalkylene group.
  • the fluorine-containing alkylene group having an ether bond preferably has 3 or more carbon atoms. Further, the number of carbon atoms of the fluorine-containing alkylene group having an ether bond is preferably 60 or less, more preferably 30 or less, still more preferably 12 or less.
  • fluorine-containing alkylene group having an ether bond examples include —CF (CF 3 ) CF 2 —O—CF (CF 3 ) — and — (CF (CF 3 ) CF 2 —O) n —CF (CF 3 )-(in the formula, n is an integer of 1 to 10), -CF (CF 3 ) CF 2 -O-CF (CF 3 ) CH 2 -,-(CF (CF 3 ) CF 2 -O) n- CF (CF 3 ) CH 2 — (where n is an integer of 1 to 10), —CH 2 CF 2 CF 2 O—CH 2 CF 2 CH 2 —, —CF 2 CF 2 CF 2 O—CF 2 CF 2- , —CF 2 CF 2 CF 2 O—CF 2 CF 2 CH 2 —, —CF 2 CF 2 O—CF 2 —, —CF 2 CF 2 O—CF 2 CH 2 — and the like can be mentioned.
  • A is —COOM, —SO 3 M, —OSO 3 M or —C (CF 3 ) 2 OM
  • M is —H, a metal atom, —NR 7 4 or a substituent. It is imidazolium which may have, pyridinium which may have a substituent, or phosphonium which may have a substituent, and R 7 is H or an organic group. R 7 is preferably an H or C 1-10 organic group, more preferably an H or C 1-4 organic group, and even more preferably an H or C 1-4 alkyl group.
  • the metal atom include alkali metals (group 1) and alkaline earth metals (group 2), and Na, K or Li is preferable.
  • —H, a metal atom or —NR 7 4 is preferable, —H, an alkali metal (Group 1), an alkaline earth metal (Group 2) or —NR 7 4 is more preferable, —H, —Na , -K, -Li or -NH 4 are more preferable, -Na, preferably from -K or -NH 4 further particularly preferred -Na or -NH 4, -NH 4 is most preferred.
  • A —COOM or —SO 3 M is preferable, and —COOM is more preferable.
  • Examples of the monomer represented by the general formula (1) include the following formula (1a): CX 2 ⁇ CFCF 2 —O— (CF (CF 3 ) CF 2 O) n5 —CF (CF 3 ) —A (1a) (In the formula, each X is the same and represents F or H. n5 represents 0 or an integer of 1 to 10, and A is the same as the above definition.) It In the above formula (1a), n5 is preferably 0 or an integer of 1 to 5, more preferably 0, 1 or 2, from the viewpoint that PTFE particles having a small primary particle size can be obtained. Or more preferably 1.
  • the above A is preferably —COOM from the viewpoint of obtaining appropriate water solubility and surface activity, and the above M is less likely to remain as an impurity, and the heat resistance of the obtained composition and a stretched body obtained from the composition is high. From the viewpoint of improving the property, H or NH 4 is preferable.
  • the polymer (1) may be a homopolymer of the fluoroallyl ether compound represented by the general formula (1a) or a copolymer with another monomer.
  • the polymer unit (1) is preferably a polymer unit (1A) based on a monomer represented by the following general formula (1A).
  • CH 2 CF (-CF 2 -O-Rf-A) (1A) (In the formula, Rf and A are the same as above.)
  • the polymer (1) may be a homopolymer of the monomer represented by the general formula (1A) or a copolymer with another monomer.
  • Z 1 is F or CF 3 ; Z 2 and Z 3 are H or F, respectively; Z 4 is H, F or CF 3 ; p1 + q1 + r1 is an integer of 0 to 10; s1 is 0 or 1, and t1 is 0.
  • examples of the monomer represented by the general formula (1) also include a monomer represented by the following formula.
  • CF 2 CFCF 2 -O-Rf-A
  • CF 2 CF-Rf-A
  • the polymer (I) is also preferably a polymer (2) containing a polymerized unit (2) based on the monomer represented by the general formula (2).
  • CX 2 CY (-O-Rf-A) (2)
  • X is the same or different and is —H or F
  • Y is —H, —F, an alkyl group or a fluorine-containing alkyl group
  • Rf is a fluorine-containing alkylene group having 1 to 40 carbon atoms, Alternatively, it is a fluorine-containing alkylene group having an ether bond having 2 to 100 carbon atoms, and A is the same as the above.
  • X is -H or -F.
  • X may be both -F, or at least one may be -H.
  • one may be -F and the other may be -H, or both may be -H.
  • Y is —H, —F, an alkyl group or a fluorine-containing alkyl group.
  • the alkyl group is an alkyl group that does not contain a fluorine atom, and may have 1 or more carbon atoms.
  • the alkyl group preferably has 6 or less carbon atoms, more preferably 4 or less carbon atoms, and even more preferably 3 or less carbon atoms.
  • the fluorine-containing alkyl group is an alkyl group containing at least one fluorine atom, and may have one or more carbon atoms.
  • the fluorine-containing alkyl group preferably has 6 or less carbon atoms, more preferably 4 or less carbon atoms, and even more preferably 3 or less carbon atoms.
  • —H, —F or —CF 3 is preferable, and —F is more preferable.
  • At least one of X and Y preferably contains a fluorine atom.
  • X can be -H and Y and Z can be -F.
  • Rf is a fluorine-containing alkylene group having 1 to 40 carbon atoms or a fluorine-containing alkylene group having 2 to 100 carbon atoms and having an ether bond.
  • the above-mentioned fluorine-containing alkylene group having an ether bond having 2 to 100 carbon atoms is an alkylene group which does not include a structure in which an oxygen atom is a terminal and which contains an ether bond between carbon atoms.
  • the fluorine-containing alkylene group of Rf preferably has 2 or more carbon atoms. Further, it is preferably 30 or less, more preferably 20 or less, still more preferably 10 or less. Examples of the fluorine-containing alkylene group, -CF 2 -, - CH 2 CF 2 -, - CF 2 CF 2 -, - CF 2 CH 2 -, - CF 2 CF 2 CH 2 -, - CF (CF 3) -, -CF (CF 3) CF 2 - , - CF (CF 3) CH 2 - and the like.
  • the fluorinated alkylene group is preferably a perfluoroalkylene group.
  • the monomer represented by the general formula (2) is at least selected from the group consisting of the monomers represented by the general formulas (2a), (2b), (2c), (2d) and (2e).
  • One kind is preferable.
  • CF 2 CF-O- (CF 2 ) n1- A (2a) (In the formula, n1 represents an integer of 1 to 10, and A is the same as above.)
  • CF 2 CF-O- (CF 2 C (CF 3 ) F) n2- A (2b) (In the formula, n2 represents an integer of 1 to 5, and A is as defined above.)
  • CF 2 CF-O- (CFX 1 ) n3- A (2c) (In the formula, X 1 represents F or CF 3 , n3 represents an integer of 1 to 10, and A is the same as the above definition.)
  • CF 2 CF-O- (CF 2 CFX 1 O) n4 - (CF 2) n6 -A (2d) (In the formula, n
  • n1 is preferably an integer of 5 or less, and more preferably an integer of 2 or less.
  • Examples of the monomer represented by the general formula (2a) include CF 2 ⁇ CF—O—CF 2 COOM, CF 2 ⁇ CF (OCF 2 CF 2 COOM), and CF 2 ⁇ CF (OCF 2 CF 2 CF). 2 COOM) (wherein M is as defined above).
  • n2 is preferably an integer of 3 or less in view of dispersion stability of the obtained composition.
  • n3 is preferably an integer of 5 or less from the viewpoint of water solubility
  • the above A is preferably —COOM
  • the above M is preferably H or NH 4.
  • X 1 is preferably —CF 3 in terms of dispersion stability of the composition
  • n4 is preferably an integer of 5 or less in terms of water solubility
  • A is A.
  • —COOM is preferably H or NH 4 .
  • Examples of the monomer represented by the general formula (2d) include CF 2 ⁇ CFOCF 2 CF (CF 3 ) OCF 2 CF 2 COOM, CF 2 ⁇ CFOCF 2 CF (CF 3 ) OCF 2 COOM, CF 2 ⁇ CFOCF 2 CF (CF 3) OCF 2 CF 2 CF 2 COOM (wherein, M represents, H, represents the NH 4 or an alkali metal.) and the like.
  • n5 is preferably an integer of 5 or less in terms of water solubility
  • A is preferably —COOM
  • M is preferably H or NH 4 .
  • Examples of the monomer represented by the general formula (2e) include CF 2 ⁇ CFOCF 2 CF 2 CF 2 COOM (wherein M represents H, NH 4 or an alkali metal).
  • the polymer (I) is a polymer (3) containing a polymerized unit (3) based on the monomer represented by the general formula (3).
  • CX 2 CY (-Rf-A) (3)
  • X is the same or different and is -H or -F
  • Y is -H, -F, an alkyl group or a fluorine-containing alkyl group
  • Rf is a fluorine-containing alkylene group having 1 to 40 carbon atoms.
  • A is the same as the above.
  • the fluorine-containing alkylene group having 2 to 100 carbon atoms and having an ether bond is an alkylene group that does not include a structure in which an oxygen atom is a terminal and that contains an ether bond between carbon atoms.
  • Rf is preferably a fluorine-containing alkylene group having 1 to 40 carbon atoms.
  • at least one of X and Y preferably contains a fluorine atom.
  • A is preferably —SO 3 M or —COOM
  • M is H, a metal atom, NR 7 4 , an imidazolium which may have a substituent, Pyridinium which may have a substituent or phosphonium which may have a substituent is preferable.
  • R 7 represents H or an organic group.
  • n1 is preferably an integer of 5 or less, and more preferably an integer of 2 or less.
  • A is preferably —COOM and M is preferably H or NH 4 .
  • Examples of the monomer represented by the general formula (3a) include CF 2 ⁇ CFCF 2 COOM (wherein M is as defined above).
  • n2 is preferably an integer of 3 or less in view of dispersion stability of the resulting composition, A is preferably —COOM, M is H or NH 4 Is preferred.
  • the polymer (I) is a polymer containing a polymer unit (4) based on at least one monomer selected from the group consisting of monomers represented by the general formulas (4a) and (4b). It is also preferable that it is (4).
  • CF 2 CF-CF 2 -O-Q F1 -CF (-Q F2- CZ 1 Z 2- A) 2 (4a) (In the formula, Z 1 , Z 2 and A are the same as defined above, and Q F1 and Q F2 are the same or different and are a single bond or a fluorine-containing alkylene group or carbon which may contain an ether bond between carbon and carbon.
  • CF 2 CF-O-Q F1 -CF (-Q F2- CZ 1 Z 2- A) 2 (4b) (Wherein Z 1 , Z 2 , A, Q F1 and Q F2 are the same as defined above)
  • Examples of the monomer represented by the general formula (4a) and the general formula (4b) include Etc.
  • the polymer (I) is preferably at least one selected from the group consisting of the polymer (1), the polymer (2) and the polymer (3), more preferably the polymer (1).
  • the polymer (I) may be a homopolymer consisting only of the polymerized unit (I), or may be copolymerized with the polymerized unit (I) and the monomer represented by the general formula (I). It may be a copolymer containing a polymerized unit based on the above monomer. From the viewpoint of solubility in the polymerization medium, a homopolymer consisting only of the polymerization unit (I) is preferable.
  • the polymerized units (I) may be the same or different at each occurrence, and the polymer (I) is a polymerized unit (I) based on two or more different monomers represented by the general formula (I). May be included.
  • the polymer unit based on the other monomer is a polymer unit based on tetrafluoroethylene.
  • the polymer units based on the other monomer may be the same or different in each occurrence, and the polymer (I) may include polymer units based on two or more different other monomers. Good.
  • Examples of the other monomer include those represented by the following formula (n1-2):
  • Rf 3 is a monomer represented by a C1-C40 fluorine-containing alkyl group or a C2-C100 fluorine-containing alkyl group having an ether bond).
  • CH 2 CFCF 2 -O-Rf 3
  • CF 2 CF-O-Rf 3
  • CF 2 CFCF 2 -O-Rf 3
  • CF 2 CF-Rf 3
  • Rf 3 Rf 3 and CH 2 ⁇ CH—O—Rf 3 (wherein Rf 3 is the same as the above formula (n1-2)).
  • Examples of the other monomer include those represented by the formula (n2-1):
  • Rf 4 is a fluorine-containing alkyl group having 1 to 40 carbon atoms or a fluorine-containing alkyl group having 2 to 100 carbon atoms and having an ether bond). Monomers are also included.
  • the Rf 4 group is
  • e6 is an integer of 1 to 10.
  • CH 2 CHCH 2 O-Rf 6 (n2-3)
  • Rf 6 is a fluorine-containing alkyl group having 1 to 40 carbon atoms or a fluorine-containing alkyl group having 2 to 100 carbon atoms and having an ether bond
  • CH 2 CH-Rf 7 (n2-4)
  • Rf 7 is a fluorine-containing alkyl group having 1 to 40 carbon atoms or a fluorine-containing alkyl group having 2 to 100 carbon atoms and having an ether bond).
  • the polymer (I) usually has a terminal group.
  • the end group is an end group generated during polymerization, and typical end groups are independently hydrogen, iodine, bromine, a chain or branched alkyl group, and a chain or branched fluoroalkyl group. It may be selected and may optionally contain at least one catenary heteroatom.
  • the alkyl group or fluoroalkyl group preferably has 1 to 20 carbon atoms.
  • the content of the polymerized units (I) is preferably 1.0 mol% or more, more preferably 3.0 mol% or more, still more preferably 5.0 mol% or more, based on all polymerized units. 10 mol% or more is still more preferable, 20 mol% or more is particularly preferable, and 30 mol% or more is particularly preferable. Further, the content of the polymer unit (I) in the polymer (I) is preferably 30 mol% or more based on all polymer units. More preferably, it is 40 mol% or more, still more preferably 60 mol% or more, even more preferably 80 mol% or more, particularly preferably 90 mol% or more, substantially 100 mol%. % Is particularly preferred. Further, the polymer (I) most preferably consists of the polymerized units (I) only.
  • the content of polymerized units based on another monomer copolymerizable with the monomer represented by the general formula (I) is 99.0 mol% or less based on all polymerized units. Is preferred, 97.0 mol% or less is more preferred, 95.0 mol% or less is still more preferred, 90 mol% or less is still more preferred, and 80 mol% or less is particularly preferred. Further, in the polymer (I), the content of the polymerized units based on another monomer copolymerizable with the monomer represented by the general formula (I) is 70 mol% or less based on all the polymerized units.
  • the polymer (I) does not contain a polymerized unit based on another monomer copolymerizable with the monomer represented by the general formula (I).
  • the polymer (I) has a number average molecular weight of preferably 0.1 ⁇ 10 4 or more, more preferably 0.2 ⁇ 10 4 or more, still more preferably 0.3 ⁇ 10 4 or more, and 0.4 ⁇ 10 4
  • the above is particularly preferable, 0.5 ⁇ 10 4 or more is particularly preferable, 1.0 ⁇ 10 4 or more is particularly preferable, and 3.0 ⁇ 10 4 or more is the most preferable.
  • the number average molecular weight of the polymer (I) is also preferably 3.1 ⁇ 10 4 or more.
  • the number average molecular weight of the polymer (I) is also preferably 75.0 ⁇ 10 4 or less, more preferably 50.0 ⁇ 10 4 or less, further preferably 40.0 ⁇ 10 4 or less, and 30.0 ⁇ 10 4.
  • the number average molecular weight and the weight average molecular weight described later are values calculated by gel permeation chromatography (GPC) using monodisperse polystyrene as a standard.
  • the number average molecular weight of the polymer (I) is determined by the correlation between the melt flow rate and the number average molecular weight calculated from the number of terminal groups obtained by NMR, FT-IR, etc. You can ask.
  • the melt flow rate can be measured according to JIS K 7210.
  • the polymer (I) has a weight average molecular weight of preferably 0.2 ⁇ 10 4 or more, more preferably 0.4 ⁇ 10 4 or more, still more preferably 0.6 ⁇ 10 4 or more, and 0.8 ⁇ 10 4
  • the above is particularly preferable, and 1.0 ⁇ 10 4 or more is particularly preferable.
  • the weight average molecular weight of the polymer (I) is 5.0 ⁇ 10 4 or more, 10.0 ⁇ 10 4 or more, 15.0 ⁇ 10 4 or more, 20.0 ⁇ 10 4 or more, or 25.0 ⁇ 10 4. It is also preferably 4 or more.
  • the weight average molecular weight of the polymer (I) is also preferably 150.0 ⁇ 10 4 or less, more preferably 100.0 ⁇ 10 4 or less, further preferably 60.0 ⁇ 10 4 or less, and 50.0 ⁇ 10 4. 4 or less is more preferable, and 40.0 ⁇ 10 4 or less is particularly preferable.
  • the polymer (I) preferably has an ion exchange rate (IXR) of 53 or less.
  • IXR is defined as the number of carbon atoms in the polymer backbone to the ionic groups.
  • Precursor groups that become ionic upon hydrolysis eg, —SO 2 F are not considered ionic groups for purposes of determining IXR.
  • IXR is preferably 0.5 or more, more preferably 1 or more, still more preferably 3 or more, even more preferably 4 or more, particularly preferably 5 or more, particularly preferably 8 or more. Further, IXR is more preferably 43 or less, further preferably 33 or less, and particularly preferably 23 or less.
  • the ion exchange capacity of the polymer (I) is, in a preferable order, 0.80 meg / g or more, 1.50 meg / g or more, 1.75 meg / g or more, 2.00 meg / g or more, 2.50 meg / g or more, It is 2.60 meg / g or more, 3.00 meg / g or more, and 3.50 meg / g or more.
  • the ion exchange capacity is the content of the ionic group (anionic group) of the polymer (I) and can be calculated from the composition of the polymer (I).
  • the ionic group (anionic group) is typically distributed along the polymer main chain.
  • the polymer (I) preferably contains a polymer main chain together with a repeating side chain bonded to the main chain, and the side chain preferably has an ionic group.
  • Polymer (I) preferably comprises ionic groups having a pKa of less than 10, more preferably less than 7.
  • the ionic groups of polymer (I) are preferably selected from the group consisting of sulfonates, carboxylates, phosphonates and phosphates.
  • sulfonate, carboxylate, phosphonate, and phosphate are intended to refer to the respective salts, or the respective acids capable of forming salts. If a salt is used, it is preferably an alkali metal salt or an ammonium salt.
  • a preferred ionic group is a sulfonate group.
  • the polymer (I) is preferably water-soluble.
  • Water-soluble means the property of being easily dissolved or dispersed in an aqueous medium.
  • the particle size of the water-soluble polymer (I) cannot be measured by, for example, the dynamic light scattering method (DLS).
  • the particle size of the water-insoluble polymer (I) can be measured by, for example, the dynamic light scattering method (DLS).
  • the polymer (I) can be produced by a conventionally known method except that the above monomer is used.
  • the content of the dimer and trimer of the monomer represented by the general formula (I) in the composition is preferably 1.0% by mass or less, more preferably 0% by mass based on the polymer (I). 0.1 mass% or less, more preferably 0.01 mass% or less, particularly preferably 0.001 mass% or less, and most preferably 0.0001 mass% or less.
  • the content of the dimer and trimer of the monomer represented by the general formula (I) in the composition can be measured by the same method as the content of the dimer and trimer in the polymer (I) described later.
  • compositions of the present disclosure have a standard specific gravity (SSG) of 2.200 or less.
  • SSG standard specific gravity
  • the standard specific gravity is preferably 2.195 or less, more preferably 2.190 or less, and even more preferably 2.185 or less.
  • the lower limit of the standard specific gravity is not limited, but is, for example, 2.130.
  • the standard specific gravity is measured by a water displacement method according to ASTM D792 using a sample molded according to ASTM D489589.
  • the content of the polymer (I) is preferably 0.0001 mass% or more and 20 mass% or less with respect to polytetrafluoroethylene.
  • the lower limit of the content of the polymer (I) is more preferably 0.001% by mass, further preferably 0.01% by mass, and 0.1% by mass with respect to polytetrafluoroethylene.
  • the upper limit is more preferably 10% by mass, further preferably 6% by mass, even more preferably 4% by mass, particularly preferably 2% by mass or less, particularly preferably 1.5% by mass or less, and 1% by mass or less.
  • the content of the polymer (I) contained in the composition of the present disclosure is determined by solid-state NMR measurement.
  • JP-A No. 11-181009 The measuring method of each polymer described in JP-A No. 11-181009 is described. As the method for measuring the content of the polymer (I), the method for measuring each polymer described therein can be used.
  • the composition of the present disclosure has an extrusion pressure of preferably 40.0 MPa or less, more preferably 35.0 MPa or less, more preferably 30.0 MPa or less, preferably 5.0 MPa or more, and 8.0 MPa or more. Is preferable, and it is more preferable that it is 10.0 MPa or more.
  • the extrusion pressure is a value obtained by the following method according to the method described in JP-A-2002-201217. To 100 g of the powder of the composition of the present disclosure, 21.7 g of a lubricant (trade name: Isopar H (registered trademark), manufactured by Exxon) is added, and mixed in a glass bottle for 3 minutes at room temperature.
  • the glass bottle is then left at room temperature (25 ° C) for at least 1 hour before extrusion to obtain the lubricated resin.
  • the lubricant resin is extruded through an orifice (diameter: 2.5 mm, land length: 11 mm, introduction angle: 30 °) at room temperature at a reduction ratio of 100: 1 to obtain a uniform beading.
  • the extrusion speed, or ram speed is 20 inches / minute (51 cm / minute).
  • the extrusion pressure is a value obtained by measuring the load when the extrusion load is in an equilibrium state in the paste extrusion and dividing the load by the cross-sectional area of the cylinder used for the paste extrusion.
  • the breaking strengths A to D are values obtained by the following method according to the method described in JP-A-2002-201217.
  • the composition of the present disclosure preferably has a breaking strength A of 10.0 N or more.
  • the breaking strength A is more preferably 13.0 N or more, still more preferably 16.0 N or more, still more preferably 19.0 N or more. Further, it is preferably 20.0 N or more, more preferably 21.0 N or more, further preferably 22.0 N or more, further preferably 25.0 N or more, 28.0 N
  • the above is particularly preferable, and the above is particularly preferably 30.0 N or more.
  • the higher the breaking strength A, the better, but the upper limit of the breaking strength A may be, for example, 100 N or less, 80.0 N or less, and 50.0 N.
  • the term “breaking strength” simply means “breaking strength A”.
  • the breaking strength A is a value obtained by the following method. First, a stretching test A of an extrusion bead is performed by the following method, and a sample for measuring breaking strength A is prepared.
  • the composition of the present disclosure is heat treated at 210 ° C. To 100 g of the powder obtained by heat treatment, 21.7 g of a lubricant is added and mixed in a glass bottle at room temperature for 3 minutes. The glass bottle is then left at room temperature (25 ° C) for at least 1 hour before extrusion to obtain the lubricated resin.
  • the lubricant resin is extruded through an orifice (diameter: 2.5 mm, land length: 11 mm, introduction angle: 30 °) at room temperature at a reduction ratio of 100: 1 to obtain a uniform beading.
  • the extrusion speed, or ram speed is 20 inches / minute (51 cm / minute).
  • the bead obtained by the above paste extrusion is heated at 230 ° C. for 30 minutes to remove the lubricant from the bead.
  • the bead (extruded body) is cut to an appropriate length, each end is fixed to a clamp so that the clamp interval is 1.5 inches (38 mm), and the bead is heated to 300 ° C. in an air circulation furnace. ..
  • the clamps are then released at the desired speed (stretch speed) until the separation distance corresponds to the desired stretch (total stretch) and a stretching test is performed.
  • This stretching method essentially follows the method disclosed in US Pat. No. 4,576,869, except that the extrusion speed (51 cm / min instead of 84 cm / min) is different.
  • "Stretch" is an increase in length due to stretching and is usually expressed as a ratio to the original length. In the above manufacturing method, the stretching speed is 1000% / sec, and the total stretching is 2400%.
  • the stretched bead obtained in the stretching test A (produced by stretching the bead) was clamped and fixed in a movable jaw having a gauge length of 5.0 cm, and pulled at 25 ° C. at a speed of 300 mm / min. A test is conducted, and the strength at the time of breaking is designated as breaking strength A.
  • the composition of the present disclosure preferably has a breaking strength B of 10.0 N or more.
  • the breaking strength B is 13.0N or higher, 15.0N or higher, 18.0N or higher, 20.0N or higher, 22.0N or higher, 25.0N or higher, 28.0N or higher, or 30.0N or higher.
  • the higher the breaking strength B, the better, but the upper limit of the breaking strength B may be, for example, 100 N or less, 80.0 N or less, and 50.0 N or less.
  • the breaking strength B is the strength measured in the same manner as the breaking strength A except that a clamp interval is 2.0 inches (51 mm) and a stretched bead obtained by changing the stretching speed to 100% / sec is used. Is.
  • the composition of the present disclosure preferably has a breaking strength C of 10.0 N or more.
  • the breaking strength C is 15.0N or more, 20.0N or more, 22.0N or more, 25.0N or more, 28.0N or more, 30.0N, 33.0N, 35.0N or more in a preferable order.
  • the higher the breaking strength C, the better, but the upper limit of the breaking strength C may be, for example, 100 N or less, 80.0 N or less, and 50.0 N or less.
  • the breaking strength C is the strength measured in the same manner as the breaking strength A except that the powder obtained by heat treatment at 240 ° C. is used.
  • the composition of the present disclosure preferably has a breaking strength D of 10.0 N or more.
  • the breaking strength D is 13.0N or more, 16.0N or more, 20.0N or more, 22.0N or more, 25.0N or more, 28.0N or more, 30.0N, 35.0N or more in order of preference. ..
  • the breaking strength D was obtained by using a powder obtained by heat treatment at 240 ° C., using a stretch bead obtained by changing the clamp interval to 2.0 inches (51 mm) and the stretching speed to 100% / sec. It is the strength measured in the same manner as the measurement of the breaking strength A.
  • the stress relaxation time is a value obtained by the following method based on the method described in JP-A-2002-201217.
  • the composition of the present disclosure preferably has a stress relaxation time of 50 seconds or longer, more preferably 80 seconds or longer, further preferably 100 seconds or longer, and may be 150 seconds or longer.
  • the stress relaxation time is a value measured by the following method. Both ends of the stretched bead obtained in the above stretching test A are connected to a fixture to form a tightly stretched bead sample having a length of 8 inches (20 cm). Keep the oven at 390 ° C and insert the fixture into the oven through the (covered) slits on the side of the oven. The time required for the bead sample to rupture after being inserted into the oven is defined as the stress relaxation time.
  • the composition of the present disclosure is preferably stretchable.
  • "stretchable" is judged based on the following criteria.
  • a lubricant trade name: Isopar H (registered trademark), manufactured by Exxon
  • Isopar H registered trademark
  • the glass bottle is then left at room temperature (25 ° C) for at least 1 hour before extrusion to obtain the lubricated resin.
  • the lubricating resin is extruded through an orifice (diameter 2.5 mm, land length 11 mm, introduction angle 30 °) at room temperature with a reduction ratio of 100: 1 to obtain a uniform bead.
  • the extrusion speed is 20 inches / minute (51 cm / minute).
  • the lubricant is removed from the beads by heating the beads obtained by paste extrusion at 230 ° C. for 30 minutes.
  • the bead (extruded product) was cut into an appropriate length, each end was fixed to a clamp so that the clamp interval was 1.5 inches (38 mm), and the temperature was raised to 300 ° C. in an air circulation furnace. To heat.
  • the clamps are then released at the desired speed (stretch speed) until the separation distance corresponds to the desired stretch (total stretch) and a stretch test is performed.
  • This stretching method essentially follows the method disclosed in US Pat. No.
  • a fluorinated surfactant is contained.
  • a composition containing a fluorine-containing surfactant and PTFE has an advantage that it can be stably produced with high productivity using a fluorine-containing surfactant.
  • the composition of the present disclosure preferably contains substantially no fluorine-containing surfactant.
  • the phrase “substantially free of a fluorine-containing surfactant” means that the fluorine-containing surfactant is 1 mass ppm or less with respect to polytetrafluoroethylene, and preferably 100%.
  • the mass is ppb or less, more preferably 10 mass ppb or less, still more preferably 1 mass ppb or less, and particularly preferably the fluorine-containing surface activity measured by liquid chromatography-mass spectrometry (LC / MS).
  • the agent is below the detection limit.
  • the amount of the above-mentioned fluorine-containing surfactant can be quantified by a known method.
  • the obtained aqueous dispersion or powder is extracted in an organic solvent of methanol, and the molecular weight information of the extract is extracted from the LC / MS / MS spectrum to confirm the conformity with the structural formula of the candidate surfactant.
  • an aqueous solution having a concentration of 5 levels or more of the confirmed surfactant is prepared, and LC / MS analysis of each concentration is performed to prepare a calibration curve with the area area.
  • the obtained aqueous dispersion or powder can be subjected to Soxhlet extraction with methanol, and the extract can be quantitatively measured by performing LC / MS analysis.
  • the extraction solvent may be acetone as well as methanol.
  • the extraction method may be a Soxhlet extraction method.
  • the content of the fluorine-containing surfactant can be quantified by LC / MS / MS analysis, for example.
  • methanol is added to the composition for extraction, and the obtained extract is subjected to LC / MS / MS analysis.
  • Soxhlet extraction, ultrasonic treatment or the like may be performed.
  • the molecular weight information is extracted to confirm the agreement with the structural formula of the candidate fluorine-containing surfactant.
  • an aqueous solution containing 5 or more levels of the confirmed fluorine-containing surfactant was prepared, and LC / MS / MS analysis was performed on the aqueous solution of each content to determine the content and the area area for the content. Plot the relationship and draw a calibration curve. Then, using the calibration curve, the area area of the LC / MS / MS chromatogram of the fluorinated surfactant in the extract can be converted into the content of the fluorinated surfactant.
  • the above-mentioned fluorine-containing surfactant is a surfactant containing a fluorine atom having a molecular weight of 800 or less.
  • fluorinated surfactant examples include fluorinated surfactants having a LogPOW of 3.5 or less.
  • the Log POW is a partition coefficient between 1-octanol and water, and Log P [wherein P is the octanol in the octanol / water (1: 1) mixed solution containing the fluorine-containing surfactant in phase separation).
  • P is the octanol in the octanol / water (1: 1) mixed solution containing the fluorine-containing surfactant in phase separation.
  • fluorine-containing surfactant examples include U.S. Patent Application Publication No. 2007/0015864, U.S. Patent Application Publication No. 2007/0015865, U.S. Patent Application Publication No. 2007/0015866, and U.S. Patents. Application Publication No. 2007/0276103, U.S. Patent Application Publication No. 2007/0117914, U.S. Patent Application Publication No. 2007/142541, U.S. Patent Application Publication No. 2008/0015319, U.S. Patent No. 3,250,808. No., U.S. Pat. No. 3,271,341, Japanese Patent Laid-Open No. 2003-119204, International Publication No. 2005/042593 pamphlet, International Publication No.
  • the fluorinated surfactant examples include anionic fluorinated surfactant.
  • the anionic fluorine-containing surfactant may be, for example, a surfactant containing a fluorine atom having a total carbon number of 20 or less in the portion excluding the anionic group.
  • the fluorine-containing surfactant may be a surfactant containing fluorine having a molecular weight of 800 or less in the anionic portion.
  • the "anionic portion” means the portion of the fluorine-containing surfactant excluding the cation.
  • F (CF 2 ) n1 COOM represented by the formula (I) described later, it is a part of “F (CF 2 ) n1 COO”.
  • anionic fluorine-containing surfactant examples include those represented by the general formula (N 0 ): X n0- Rf n0- Y 0 (N 0 ) (In the formula, X n0 is H, Cl or and F. Rf n0 has a carbon number of 3 to 20, and is a chain, branched chain or ring, and part or all of H is substituted with F. An alkylene group, the alkylene group may contain one or more ether bonds, and a part of H may be substituted with Cl. Y 0 is an anionic group. Can be mentioned.
  • the anionic group of Y 0 may be —COOM, —SO 2 M, or —SO 3 M, or —COOM or —SO 3 M.
  • M is H, a metal atom, NR 7 4 , imidazolium which may have a substituent, pyridinium which may have a substituent or phosphonium which may have a substituent, and R 7 Is H or an organic group.
  • the metal atom include alkali metals (group 1), alkaline earth metals (group 2), and the like, such as Na, K, or Li.
  • R 7 may be an H or C 1-10 organic group, an H or C 1-4 organic group, or an H or C 1-4 alkyl group.
  • M may be H, a metal atom or NR 7 4 and may be H, an alkali metal (Group 1), an alkaline earth metal (Group 2) or NR 7 4 , H, Na, K, Li or It may be NH 4 .
  • Rf n0 may be one in which 50% or more of H is replaced by fluorine.
  • Examples of the compound represented by the general formula (N 0 ) include the general formula (N 1 ): X n0- (CF 2 ) m1- Y 0 (N 1 ) (In the formula, X n0 is H, Cl and F, m 1 is an integer of 3 to 15, and Y 0 is as defined above.), A compound represented by the general formula (N 2 ).
  • Rf n1 is a perfluoroalkyl group having 1 to 5 carbon atoms
  • m2 is an integer of 0 to 3
  • X n1 is F or CF 3
  • Y 0 is as defined above.
  • Rf n2 is a partially or fully fluorinated alkyl group which may contain an ether bond having 1 to 13 carbon atoms
  • m3 is an integer of 1 to 3
  • Rf n3 is a linear chain.
  • N 4 a compound represented by the general formula (N 4 ).
  • Rf n4 is a linear or branched partially or fully fluorinated alkyl group which may contain an ether bond having 1 to 12 carbon atoms, and Y n1 and Y n2 are the same or different.
  • X n2 , X n3 and X n4 may be the same or different, and may be H, F, or a linear or branched part or complete which may contain an ether bond having 1 to 6 carbon atoms.
  • Rf n5 is a linear or branched partially or completely fluorinated alkylene group which may contain an ether bond having 1 to 3 carbon atoms, and Lf is a linking group.
  • Y 0 are defined as above, provided that a compound represented by X n2 , X n3 , X n4 and Rf n5 has a total carbon number of 18 or less.
  • anionic surfactants include carboxylic acid-based surfactants and sulfonic acid-based surfactants.
  • These surfactants include perfluorocarboxylic acid represented by the following general formula (I).
  • (I) ⁇ -H perfluorocarboxylic acid (II) represented by the following general formula (II), perfluoropolyether carboxylic acid (III) represented by the following general formula (III), and general formula (IV ),
  • a perfluoroalkylalkylenecarboxylic acid (IV) an alkoxyfluorocarboxylic acid (V) represented by the following general formula (V), and a perfluoroalkylsulfonic acid (VI) represented by the following general formula (VI).
  • ⁇ -H perfluorosulfonic acid represented by the following general formula (VII)
  • perfluoroalkylalkylene sulfonic acid (VIII) represented by the following general formula (VIII)
  • general formula (IX) Alkyl alkylene carboxylic acid (IX) represented, fluorocarboxylic acid (X) represented by the following general formula (X), alkoxyfluoro sulfonic acid (XI) represented by the following general formula (XI), the following general formula ( The compound (XII) represented by XII), the compound (XIII) represented by the following general formula (XIII) and the like can be mentioned.
  • the perfluorocarboxylic acid (I) is represented by the following general formula (I) F (CF 2 ) n1 COOM (I) (Wherein, n1 is 3 is an integer of ⁇ 14, M is H, a metal atom, NR 7 4, which may imidazolium substituted, pyridinium which may have a substituent or It is a phosphonium which may have a substituent, and R 7 is represented by H or an organic group.).
  • ⁇ -H perfluorocarboxylic acid is represented by the following general formula (II) H (CF 2 ) n2 COOM (II) (In the formula, n2 is an integer of 4 to 15, and M is as defined above.).
  • the perfluoropolyethercarboxylic acid (III) has the following general formula (III) Rf 1 —O— (CF (CF 3 ) CF 2 O) n3 CF (CF 3 ) COOM (III) (In the formula, Rf 1 is a perfluoroalkyl group having 1 to 5 carbon atoms, n3 is an integer of 0 to 3, and M is as defined above.). ..
  • the perfluoroalkylalkylenecarboxylic acid (IV) has the following general formula (IV) Rf 2 (CH 2 ) n4 Rf 3 COOM (IV) (In the formula, Rf 2 is a perfluoroalkyl group having 1 to 5 carbon atoms, Rf 3 is a linear or branched perfluoroalkylene group having 1 to 3 carbon atoms, and n4 is 1 to 3 Is an integer and M is defined as above.).
  • the alkoxyfluorocarboxylic acid (V) has the following general formula (V): Rf 4 —O—CY 1 Y 2 CF 2 —COOM (V) (In the formula, Rf 4 is a linear or branched partially or fully fluorinated alkyl group which may contain an ether bond having 1 to 12 carbon atoms, and Y 1 and Y 2 are the same or different. , H or F, and M is as defined above.).
  • the perfluoroalkylsulfonic acid (VI) has the following general formula (VI) F (CF 2 ) n5 SO 3 M (VI) (In the formula, n5 is an integer of 3 to 14, and M is as defined above.).
  • ⁇ -H perfluorosulfonic acid has the general formula (VII): H (CF 2 ) n6 SO 3 M (VII) (In the formula, n6 is an integer of 4 to 14, and M is as defined above.).
  • the perfluoroalkylalkylene sulfonic acid (VIII) has the following general formula (VIII) Rf 5 (CH 2 ) n7 SO 3 M (VIII) (In the formula, Rf 5 is a perfluoroalkyl group of 1 to 13, n7 is an integer of 1 to 3, and M is as defined above.).
  • the alkylalkylenecarboxylic acid (IX) has the following general formula (IX): Rf 6 (CH 2 ) n8 COOM (IX) (In the formula, Rf 6 is a linear or branched partially or fully fluorinated alkyl group which may contain an ether bond having 1 to 13 carbon atoms, and n8 is an integer of 1 to 3, M is as defined above.).
  • the fluorocarboxylic acid (X) has the following general formula (X): Rf 7 -O-Rf 8 -O-CF 2 -COOM (X) (In the formula, Rf 7 is a linear or branched partially or fully fluorinated alkyl group which may contain an ether bond having 1 to 6 carbon atoms, and Rf 8 is a direct alkyl group having 1 to 6 carbon atoms. It is a chain- or branched-chain partially or completely fluorinated alkyl group, and M is as defined above.).
  • the above alkoxyfluorosulfonic acid (XI) has the following general formula (XI): Rf 9 —O—CY 1 Y 2 CF 2 —SO 3 M (XI) (In the formula, Rf 9 is a partially or fully fluorinated alkyl group which may have a linear or branched chain and may contain an ether bond having 1 to 12 carbon atoms, and Y 1 And Y 2 are the same or different and each is H or F, and M is as defined above.).
  • the compound (XII) has the following general formula (XII): (Wherein X 1 , X 2 and X 3 may be the same or different, and may be H, F and a linear or branched partial or perfluorinated chain which may contain an ether bond having 1 to 6 carbon atoms. Is an alkyl group, Rf 10 is a perfluoroalkylene group having 1 to 3 carbon atoms, L is a linking group, and Y 0 is an anionic group.). Y 0 may be —COOM, —SO 2 M, or —SO 3 M, —SO 3 M, or COOM, where M is as defined above. Examples of L include a single bond, a partially or fully fluorinated alkylene group which may contain an ether bond having 1 to 10 carbon atoms.
  • the compound (XIII) has the following general formula (XIII): Rf 11 —O— (CF 2 CF (CF 3 ) O) n9 (CF 2 O) n10 CF 2 COOM (XIII) (In the formula, Rf 11 is a fluoroalkyl group having 1 to 5 carbon atoms including chlorine, n9 is an integer of 0 to 3, n10 is an integer of 0 to 3, and M is defined as above. It is represented by). As the compound (XIII), CF 2 ClO (CF 2 CF (CF 3 ) O) n9 (CF 2 O) n10 CF 2 COONH 4 (mixture having an average molecular weight of 750, wherein n 9 and n 10 are as defined above). There is).
  • examples of the anionic fluorine-containing surfactant include a carboxylic acid surfactant and a sulfonic acid surfactant.
  • the powder of the composition of the present disclosure is preferable for molding, and suitable applications include hydraulic systems for aircraft and automobiles, tubes for fuel systems, and the like, and flexible hoses such as chemicals and steam, and wire coating applications. Can be mentioned. It can also be used as a binder for batteries and as a dustproof application.
  • the composition of the present disclosure comprises performing polymerization of tetrafluoroethylene in an aqueous medium in the presence of a polymer (I) containing a polymerized unit (I) based on a monomer represented by the general formula (I).
  • the composition of the present disclosure is obtained by polymerizing tetrafluoroethylene in an aqueous medium in the presence of a polymer (I) containing polymerized units (I) based on a monomer represented by the general formula (I).
  • the polymerization may be polymerization of tetrafluoroethylene and the above-mentioned modified monomer.
  • At least one kind of the above-mentioned polymer (I) may be used, two or more kinds of the above-mentioned polymer (I) may be used at the same time, and a molded article (having a volatile property or the above composition (for example, other compounds having a surface active ability may be used at the same time as long as they can remain in the stretched body).
  • the polymerization temperature is usually 5 to 120 ° C.
  • the polymerization pressure is 0.05 to 10 MPaG.
  • the polymerization temperature and the polymerization pressure are appropriately determined depending on the type of monomer used, the molecular weight of the target fluoropolymer, and the reaction rate.
  • the polymerization temperature is preferably 10 to 150 ° C., more preferably 30 ° C. or higher, further preferably 50 ° C. or higher, more preferably 120 ° C. or lower, still more preferably 100 ° C. or lower.
  • the polymerization pressure is preferably 0.05 to 10 MPaG, more preferably 0.3 MPaG or more, further preferably 0.5 MPaG or more, more preferably 5.0 MPaG or less, and further preferably 3. It is 0 MPaG or less.
  • the polymerization pressure is preferably 1.0 MPaG or more, more preferably 1.2 MPaG or more, still more preferably 1.5 MPaG or more, and particularly preferably 1 MPa. It is at least 0.8 MPaG, most preferably at least 2.0 MPaG.
  • the amount of the polymer (I) at the start of polymerization is preferably 1 mass ppm or more with respect to the aqueous medium.
  • the amount of the polymer (I) at the start of polymerization is preferably 10 mass ppm or more, more preferably 50 mass ppm or more, still more preferably 100 mass ppm or more, still more preferably 200 mass ppm or more. Is. Although the upper limit is not particularly limited, for example, 100,000 mass ppm is preferable, and 50,000 mass ppm is more preferable. When the amount of the polymer (I) at the start of the polymerization is within the above range, an aqueous dispersion liquid having further excellent dispersion stability can be obtained.
  • the polymer (I) is preferably added in a total amount of 0.0001 to 10% by mass based on 100% by mass of the aqueous medium.
  • a more preferable lower limit is 0.001% by mass, and a more preferable upper limit is 1% by mass. If it is less than 0.0001% by mass, the dispersing force may be insufficient, and if it exceeds 10% by mass, the effect commensurate with the added amount may not be obtained, and the polymerization rate may be lowered or the reaction may be stopped. There is.
  • the amount of the above compound added is appropriately determined depending on the type of monomer used, the molecular weight of the target fluoropolymer, and the like.
  • the aqueous medium is a reaction medium in which polymerization is performed and means a liquid containing water.
  • the aqueous medium is not particularly limited as long as it contains water, and water, for example, a fluorine-free organic solvent such as alcohol, ether, and ketone, and / or a fluorine-containing organic solvent having a boiling point of 40 ° C. or lower. May be included.
  • the above production method may include a step of adding a polymerization terminator to an aqueous medium (hereinafter, also referred to as “polymerization terminator addition step”).
  • the step of adding the polymerization terminator is performed during the polymerization step.
  • a compound having no re-initiating ability after being added or chain-transferred to a free radical in the polymerization system is used.
  • a stable radical that easily undergoes a chain transfer reaction with a primary radical or a growing radical and then generates a stable radical that does not react with a monomer, or an easy addition reaction with a primary radical or a growing radical causes a stable radical.
  • a compound having a function of generating is used.
  • the activity of a so-called chain transfer agent is generally characterized by a chain transfer constant and a re-initiating efficiency.
  • polymerization terminator examples include aromatic hydroxy compounds, aromatic amines, N, N-diethylhydroxylamine, quinone compounds, terpenes, thiocyanates, and cupric chloride (CuCl 2 ).
  • aromatic hydroxy compound examples include unsubstituted phenol, polyhydric phenol, salicylic acid, m- or p-salicylic acid, gallic acid and naphthol.
  • Examples of the above-mentioned unsubstituted phenol include o-, m- or p-nitrophenol, o-, m- or p-aminophenol, p-nitrosophenol and the like.
  • Examples of polyhydric phenols include catechol, resorcin, hydroquinone, pyrogallol, phloroglucin, naphthresorcinol and the like.
  • Examples of aromatic amines include o-, m- or p-phenylenediamine and benzidine.
  • Examples of the quinone compound include hydroquinone, o-, m- or p-benzoquinone, 1,4-naphthoquinone, and alizarin.
  • thiocyanates examples include ammonium thiocyanate (NH 4 SCN), potassium thiocyanate (KSCN), sodium thiocyanate (NaSCN), and the like.
  • NH 4 SCN ammonium thiocyanate
  • KSCN potassium thiocyanate
  • NaSCN sodium thiocyanate
  • quinone compounds are preferable, and hydroquinone is more preferable.
  • the above-mentioned polymerization terminator is preferably added before 90% by mass of all tetrafluoroethylene consumed in the polymerization reaction is polymerized. More preferably, 85% by mass, and even more preferably 80% by mass of the total tetrafluoroethylene is more preferably added before the polymerization. Further, it is preferable to add 5% by mass of all tetrafluoroethylene consumed in the polymerization reaction after polymerization, and more preferably 10% by mass after polymerization.
  • the addition amount of the above polymerization terminator is preferably an amount corresponding to 0.1 to 20 mass ppm of the mass of the aqueous medium used, and more preferably an amount corresponding to 3 to 10 mass ppm.
  • the production method includes a step of adding a decomposing agent to the aqueous medium instead of the polymerization terminator.
  • a decomposing agent By adding a decomposing agent, the radical concentration during polymerization can be adjusted.
  • the decomposer include sulfite, bisulfite, bromate, diimine, oxalic acid, copper salt, iron salt and the like.
  • the sulfite include sodium sulfite and ammonium sulfite.
  • the copper salt include copper (II) sulfate
  • examples of the iron salt include iron (II) sulfate.
  • the amount of the above decomposing agent added is in the range of 25 to 300% by mass with respect to the amount of the oxidizing agent combined as a polymerization initiator (a redox initiator described later).
  • the amount is preferably 25 to 150% by mass, more preferably 50 to 100% by mass. Further, it is preferable to add 5% by mass of all tetrafluoroethylene consumed in the polymerization reaction after polymerization, and more preferably 10% by mass after polymerization.
  • the addition amount of the above polymerization terminator is preferably an amount corresponding to 0.1 to 20 mass ppm of the mass of the aqueous medium used, and more preferably an amount corresponding to 3 to 10 mass ppm.
  • the polymer (I) In the polymerization step, it is also preferable to continuously add the polymer (I) during the polymerization of TFE.
  • the continuous addition of the polymer (I) means that the polymer (I) is not added all at once, but over time and without interruption or division. By continuously adding the polymer (I), a composition having more excellent dispersion stability can be obtained.
  • the addition amount of the polymer (I) is preferably 0.001 to 10 mass% with respect to 100 mass% of the aqueous medium.
  • a more preferable lower limit is 0.005% by mass
  • a still more preferable lower limit is 0.01% by mass
  • a more preferable upper limit is 5% by mass
  • a still more preferable upper limit is 2% by mass.
  • the polymerization step it is preferable to generate particles of 0.6 ⁇ 10 13 particles / ml or more.
  • the number of particles to be generated is, in a preferable order, 0.7 ⁇ 10 13 particles / mL or more, 0.8 ⁇ 10 13 particles / mL or more, 0.9 ⁇ 10 13 particles / mL or more, 1.0 ⁇ 10 13 particles.
  • the number of cells / mL is 1.5 ⁇ 10 13 cells / mL or more.
  • the upper limit of the number of particles to be generated is not particularly limited, but is, for example, 7.0 ⁇ 10 14 particles / mL.
  • the particles generated by the polymerization of TFE are concentrated in the first half of the polymerization and hardly generated in the second half of the polymerization. Therefore, the number of particles in the polymerization step is almost the same as the number of particles generated in the first half of the polymerization. Therefore, the number of particles in the polymerization step can be predicted by measuring the number of primary particles in the finally obtained aqueous dispersion.
  • TFE and the modified monomer it is also preferable to polymerize TFE and the modified monomer.
  • the modifying monomer those described above as those capable of being copolymerized with TFE can be used.
  • TFE and the modified monomer By polymerizing TFE and the modified monomer, primary particles having a smaller average primary particle diameter and aspect ratio can be obtained, and an aqueous dispersion having more excellent dispersion stability can be obtained.
  • the total amount of the modified monomer added when polymerizing TFE is preferably 0.00001 mass% or more, more preferably 0.0001 mass% or more, and further preferably 0.001 mass% with respect to the obtained PTFE. It is at least mass%, more preferably at least 0.005 mass%, and particularly preferably at least 0.009 mass%.
  • the total amount of the modified monomer added during the polymerization is preferably 1.0% by mass or less, 0.90% by mass or less, 0.50% by mass or less, and 0.40% by mass with respect to the obtained PTFE. Below, 0.30 mass% or less, 0.20 mass% or less, 0.15 mass% or less, 0.10 mass% or less, 0.05 mass% or less.
  • a modifying monomer copolymerizable with TFE is usually added to the reactor.
  • the modifying monomer may be added before the start of polymerization, may be added at the same time as the start of polymerization, or may be added after the start of polymerization and during the period during which nuclei of PTFE particles are formed.
  • the modifying monomer may be added at least before the polymerization reaction is started or before the polymerization reaction proceeds and the concentration of PTFE in the aqueous dispersion reaches 10.0% by mass.
  • a modifying monomer may be further added after the amount exceeds 10.0% by mass.
  • the modifying monomer may be added before the PTFE concentration reaches 10.0% by mass, and the modifying monomer may be subsequently added even if the concentration exceeds 10.0% by mass.
  • the modifying monomer may be added at least once before the concentration of PTFE reaches 10.0% by mass, and the modifying monomer may be further added at least once after exceeding 10.0% by mass.
  • TFE may be used to push the modified monomer into the reactor.
  • the amount of the monomer is preferably 0.00001 mass% or more, more preferably 0.0001 mass% or more, still more preferably 0.001 mass% or more, and particularly preferably, relative to the obtained PTFE. It is 0.003 mass% or more.
  • the amount of the modifying monomer to be used is, relative to the obtained PTFE, preferably 1.0% by mass or less, 0.90% by mass or less, 0.50% by mass or less, 0.40% by mass or less, 0.30% by mass. Below, 0.20 mass% or less, 0.15 mass% or less, 0.10 mass% or less, and 0.05 mass% or less.
  • the content of the dimer and trimer of the monomer represented by the general formula (I) (hereinafter, sometimes referred to as the monomer (I)) is similar to that of the polymer (I). On the other hand, 1.0% by mass or less of the polymer (I) may be used.
  • the composition of the present disclosure is A step of obtaining a crude composition containing a polymer of the monomer (I) by polymerizing the monomer (I) represented by the general formula (I) in an aqueous medium, and By removing the dimer and trimer of the monomer (I) contained in the crude composition from the crude composition, the content of the dimer and trimer of the monomer (I) becomes the polymer (I).
  • a step of obtaining a polymer (I) of 1.0% by mass or less A step of obtaining polytetrafluoroethylene by polymerizing tetrafluoroethylene in an aqueous medium in the presence of the polymer (I), and It is also preferable to manufacture by a manufacturing method including a step of adding a polymerization terminator to an aqueous medium.
  • the polymer (I) used in the above production method does not substantially contain the dimer and trimer of the monomer (I).
  • the dimer and trimer of the monomer (I) usually occur when the monomer (I) is polymerized to obtain the polymer (I).
  • the content of the dimer and trimer in the polymer (I) is 1.0% by mass or less, preferably 0.1% by mass or less, and more preferably 0.1% by mass or less with respect to the polymer (I).
  • the amount is 01% by mass or less, more preferably 0.001% by mass or less, and particularly preferably 0.0001% by mass or less.
  • the content of the dimer and the trimer in the polymer (I) is determined by gel permeation chromatography (GPC) analysis of the polymer (I), and the content of the dimer and the trimer with respect to the total area of each peak of the chromatogram obtained by the GPC analysis. It can be specified by calculating the total ratio of peak areas (area percentage).
  • GPC gel permeation chromatography
  • liquid chromatography-mass spectrometry (LC / MS / MS) Can be specified by measuring Specifically, an aqueous solution containing 5 or more levels of the monomer (I) is prepared, and each content is subjected to LC / MS / MS analysis to determine the content and the area area (peak area) for that content. Plot the relationship with the (integral value of) and prepare a calibration curve for the monomer (I). Furthermore, a calibration curve of the dimer and trimer of the monomer (I) is prepared from the calibration curve of the monomer (I).
  • Methanol is added to the polymer (I) to prepare a mixture, the extract (supernatant) is recovered from the mixture by centrifugation, and the obtained extract is subjected to LC / MS / MS analysis. Then, the area area (integral value of peaks) of the dimer and trimer of the monomer (I) can be converted into the content of dimer and trimer using the calibration curve.
  • the polymer (I) is a polymer containing polymerized units (I) based on the monomer (I).
  • the polymer (I) used in the present disclosure includes a polymer (I) containing two or more polymer units (I), a dimer (a polymer containing two polymer units (I)) and a trimer (three polymer units (I). A polymer containing I) is substantially removed.
  • the molecular weight of the monomer (I) is preferably 400 or less. That is, the polymer (I) preferably contains substantially no dimer or trimer having a molecular weight of 1200 or less.
  • the dimer and trimer of the polymer (I) may be a polymer formed from one kind of the monomer (I) as the monomer (I) represented by the general formula (I), It may be a copolymer formed from two or more kinds of monomers (I) having different structures.
  • the monomer (I) can be polymerized by a known method.
  • a crude composition By producing a crude composition by such a method, a crude composition in which the polymer (I) is dispersed or dissolved in an aqueous medium can be obtained.
  • the polymerization of the monomer (I) is preferably carried out substantially in the absence of a fluorine-containing surfactant (excluding the monomer (I) represented by the general formula (I)).
  • substantially in the absence of a fluorine-containing surfactant means that the amount of the fluorine-containing surfactant in the aqueous medium is 10 mass ppm or less.
  • the amount of the fluorinated surfactant with respect to the aqueous medium is preferably 1 mass ppm or less, more preferably 100 mass ppb or less, still more preferably 10 mass ppb or less, still more preferably 1 mass ppb or less. Is.
  • the crude composition thus obtained contains, as a polymer of the monomer (I), a dimer content of more than 1.0% by mass in total with respect to the mass of the polymer of the monomer (I). And trimmers are included.
  • the content of the dimer and trimer in the polymer of the monomer (I) may be, for example, 2.0% by mass or more based on the polymer of the monomer (I), and may be 3.0 It may be not less than mass%, not more than 30.0 mass%, or not more than 20.0 mass%.
  • the content of dimers and trimers in the crude composition is determined by performing gel permeation chromatography (GPC) analysis of the crude composition, and adding the peak areas of the dimers and trimers to the total area of each peak in the chromatogram obtained by GPC analysis. It can be specified by calculating the ratio (area percentage).
  • GPC gel permeation chromatography
  • the means for removing the dimer and trimer is not particularly limited, but at least one means selected from the group consisting of ultrafiltration, microfiltration and dialysis membrane treatment is preferred, and selected from the group consisting of microfiltration and dialysis membrane treatment. At least one means is more preferred, and ultrafiltration is even more preferred.
  • the existence of the dimer and trimer of the monomer (I) in the polymer (I) was revealed for the first time, and the dimer and trimer of the monomer (I) in the polymer (I) was detected by ultrafiltration. It was found for the first time that polymer (I) (crude composition) can be removed with high efficiency by at least one means selected from the group consisting of microfiltration and dialysis membrane treatment.
  • the unreacted monomer (I) When removing the dimer and trimer, the unreacted monomer (I) is usually removed from the crude composition at the same time. Even if the unreacted monomer (I) is incorporated into PTFE by the polymerization, it does not necessarily adversely affect the function of PTFE, so that the unreacted monomer (I) does not necessarily have to be removed. .. However, by removing the unreacted monomer (I) at the same time as the dimer and trimer, the amount of the monomer to be used for the polymerization can be calculated without considering the presence of the unreacted monomer (I). And has an advantage that PTFE having a desired monomer composition can be easily produced.
  • the monomer existing in the polymerization system is present.
  • the fluoromonomer (excluding the monomer (I)) occupies the majority of the polymerization system, but the dimerization and trimerization of the monomer (I) almost proceed depending on the polymerization reaction in the polymerization system. In fact, the dimers and trimers of the monomer (I) hardly remain in the obtained PTFE.
  • the crude composition obtained by polymerizing the monomer (I) may be a composition obtained by polymerization after polymerization, or a composition obtained by diluting or concentrating the composition obtained after polymerization by polymerization. Or may have been subjected to dispersion stabilization treatment or the like. In order to smoothly carry out ultrafiltration, microfiltration or dialysis membrane treatment, it is also preferable to adjust the viscosity of the crude composition by these treatments.
  • the content of the polymer of the monomer (I) in the crude composition is not particularly limited and may be, for example, 0.1 to 20% by mass.
  • the content of the polymer of the monomer (I) in the crude composition is preferably 18.0 mass% or less, and more preferably 15.0 mass% or less, from the viewpoint of removal efficiency of dimers and trimers. And more preferably 12.0 mass% or less, particularly preferably 10.0 mass% or less, preferably 0.5 mass% or more, more preferably 1.0 mass% or more, It is more preferably 1.2% by mass or more, and particularly preferably 1.5% by mass or more.
  • the content of the polymer of the monomer (I) in the crude composition is, for example, the method of adding water to the crude composition obtained by the polymerization of the monomer (I), It can be adjusted by a method of concentrating the crude composition obtained by the polymerization.
  • the pH of the crude composition is preferably 0 to 11, more preferably 0.5 to 8.0, still more preferably 1.0 to 7.0.
  • the pH of the crude composition can be adjusted by adding a pH adjuster to the crude composition obtained by polymerizing the monomer (I).
  • the pH adjuster may be an acid or an alkali, and examples thereof include phosphate, sodium hydroxide, potassium hydroxide, aqueous ammonia and the like.
  • the viscosity of the crude composition is preferably 25 mPa ⁇ s or less because ultrafiltration, microfiltration or dialysis membrane treatment proceeds smoothly.
  • the viscosity of the crude composition is, for example, a method of adjusting the number average molecular weight of the polymer of the monomer (I), a method of adjusting the concentration of the polymer of the monomer (I) in the crude composition, or a crude composition. It can be adjusted by a method of adjusting the temperature of the object.
  • the ultrafiltration or microfiltration is not limited to a cross-flow method or a dead-end method, but a cross-flow method is preferable from the viewpoint of reducing clogging of the membrane.
  • the ultrafiltration can be performed using an ultrafiltration membrane.
  • the ultrafiltration can be performed using, for example, an ultrafiltration device having an ultrafiltration membrane, and a centrifugal ultrafiltration method, a batch ultrafiltration method, a circulation ultrafiltration method, or the like can be adopted.
  • the molecular weight cut-off of the ultrafiltration membrane is usually about 0.1 ⁇ 10 4 to 30 ⁇ 10 4 Da.
  • the ultrafiltration membrane preferably has a molecular weight cutoff of 1.5 ⁇ 10 4 Da or more because it can prevent clogging of the membrane and efficiently reduce dimers and trimers.
  • the molecular weight cut off is more preferably 2.0 ⁇ 10 4 Da or more, particularly preferably 3.0 ⁇ 10 4 Da or more, and most preferably 5.0 ⁇ 10 4 Da or more.
  • the molecular weight cut off may be 8.0 ⁇ 10 4 Da or more.
  • the molecular weight cut-off is preferably 20 ⁇ 10 4 Da or less, more preferably 10 ⁇ 10 4 Da or less, from the viewpoint of efficiency of removing dimers and trimers.
  • the molecular weight cut-off of the ultrafiltration membrane can be, for example, the molecular weight that allows 90% of polystyrene having a known weight average molecular weight to pass through the membrane to be blocked. Quantification of polystyrene can be performed using gel permeation chromatography.
  • Examples of the shape of the ultrafiltration membrane include conventionally known ones and are not limited. Examples thereof include a hollow fiber type, a flat membrane type, a spiral type, and a tubular type. From the viewpoint of preventing clogging, the hollow fiber type is preferable.
  • the inner diameter of the hollow fiber type ultrafiltration membrane is not limited, but may be, for example, 0.1 to 2 mm. It is preferably 0.8 to 1.4 mm.
  • the length of the hollow fiber type ultrafiltration membrane is not limited, but may be, for example, 0.05 to 3 m. It is preferably 0.05 to 2 m.
  • the material of the ultrafiltration membrane is not particularly limited, but includes cellulose, cellulose ester, polysulfone, sulfonated polysulfone, polyether sulfone, sulfonated polyether sulfone, chlorinated polyethylene, polypropylene, polyolefin, polyvinyl alcohol, Examples thereof include organic materials such as polymethylmethacrylate, polyacrylonitrile, polyvinylidene fluoride, and polytetrafluoroethylene, metals such as stainless steel, and inorganic materials such as ceramics.
  • the material of the ultrafiltration membrane is preferably an organic material, more preferably chlorinated polyethylene, polypropylene, polyvinylidene fluoride, polytetrafluoroethylene, polyacrylonitrile, polysulfone, or polyether sulfone. Acrylonitrile or polyvinylidene fluoride is more preferred.
  • ultrafiltration membrane examples include G-5 type, G-10 type, G-20 type, G-50 type, PW type, HWS UF type from DESAL; HFM-180 and HFM- from KOCH. 183, HFM-251, HFM-300, HFM-116, HFM-183, HFM-300, HFK-131, HFK-328, MPT-U20, MPS-U20P, MPS-U20S; SPE1, SPE3, SPE5 from Synder. , SPE10, SPE30, SPV5, SPV50, SOW30; Microza (registered trademark) UF series manufactured by Asahi Kasei; NTR7410 manufactured by Nitto Denko.
  • the ultrafiltration is preferably performed at a pressure of 0.01 MPa or more from the viewpoint of efficiency of removing dimers and trimers.
  • the pressure is more preferably 0.03 MPa or more, further preferably 0.05 MPa or more. Further, the above pressure is preferably 0.5 MPa or less, more preferably 0.25 MPa or less, and further preferably 0.2 MPa or less from the viewpoint of pressure resistance.
  • the ultrafiltration is preferably performed at a flow rate of 10 mL / min or more, more preferably 50 mL / min or more, and at a flow rate of 5000 mL / min or less. It is preferable to perform it, and more preferable to perform it at a flow rate of 1000 mL / min or less.
  • the microfiltration can be performed using a microfiltration membrane.
  • the microfiltration membrane usually has an average pore size of 0.05 to 1.0 ⁇ m.
  • the microfiltration membrane preferably has an average pore diameter of 0.1 ⁇ m or more because it can efficiently remove dimers and trimers.
  • the thickness is more preferably 0.075 ⁇ m or more, still more preferably 0.1 ⁇ m or more.
  • the average pore diameter is preferably 1.00 ⁇ m or less.
  • the average pore diameter is more preferably 0.50 ⁇ m or less, and further preferably 0.25 ⁇ m or less.
  • the average pore diameter of the microfiltration membrane can be measured according to ASTM F31603 (bubble point method).
  • the shape of the microfiltration membrane is not particularly limited and may be a conventionally known one, and examples thereof include a hollow fiber type, a flat membrane type, a spiral type, and a tubular type. From the viewpoint of preventing clogging, the hollow fiber type is preferable.
  • the inner diameter of the hollow fiber type ultrafiltration membrane is not limited, but may be, for example, 0.1 to 2 mm. It is preferably 0.8 to 1.4 mm.
  • the length of the hollow fiber type ultrafiltration membrane is not limited, but may be, for example, 0.05 to 3 m. It is preferably 0.05 to 2 m.
  • Examples of the material of the microfiltration membrane include cellulose-based, aromatic polyamide, polyvinyl alcohol, polysulfone, polyether sulfone, polyvinylidene fluoride, polyethylene, polyacrylonitrile, polypropylene, polycarbonate, polytetrafluoroethylene, ceramics, metal and the like. Be done. Among them, aromatic polyamide, polyvinyl alcohol, polysulfone, polyvinylidene fluoride, polyethylene, polyacrylonitrile, polypropylene, polycarbonate or polytetrafluoroethylene are preferable, and polyacrylonitrile or polyvinylidene fluoride is particularly preferable.
  • microfiltration membrane examples include Cefit manufactured by NGK Insulators Co., Ltd .; Microsa U series, Microsa P series manufactured by Asahi Kasei; Poreflon SPMW, Poaflon OPMW, Poaflon PM manufactured by Sumitomo Electric Co .; Trefil; Micro by Toray.
  • Examples include NADIR MP005 and NADIR MV020 manufactured by Dyne Nadia; X-flow manufactured by Norit.
  • the microfiltration is preferably performed at a pressure of 0.01 MPa or more from the viewpoint of the efficiency of removing dimers and trimers.
  • the pressure is more preferably 0.03 MPa or more, further preferably 0.05 MPa or more. Further, the above pressure is preferably 0.5 MPa or less, more preferably 0.25 MPa or less, and further preferably 0.2 MPa or less from the viewpoint of pressure resistance.
  • the microfiltration is preferably performed at a flow rate of 10 mL / min or more, more preferably at 50 mL / min or more, and at 5000 mL / min or less. It is preferable that the flow rate is 1000 mL / min or less.
  • the dialysis membrane treatment is performed using a dialysis membrane.
  • the dialysis membrane usually has a molecular weight cut off of 0.05 ⁇ 10 4 to 100 ⁇ 10 4 Da.
  • the above dialysis membrane preferably has a molecular weight cutoff of 0.3 ⁇ 10 4 Da or more because it can prevent clogging of the membrane and efficiently remove dimers and trimers.
  • the molecular weight cut off is more preferably 0.5 ⁇ 10 4 Da or more, still more preferably 1.0 ⁇ 10 4 Da or more, still more preferably 1.5 ⁇ 10 4 Da or more, and 2.0 ⁇ 10 4 Da.
  • the above is particularly preferable, 3.0 ⁇ 10 4 Da or more is particularly preferable, and 5.0 ⁇ 10 4 Da or more is most preferable.
  • the molecular weight cut off may be 8.0 ⁇ 10 4 Da or more.
  • the molecular weight cut-off is preferably 20 ⁇ 10 4 Da or less, more preferably 10 ⁇ 10 4 Da or less, from the viewpoint of efficiency of removing dimers and trimers.
  • the molecular weight cut-off of the dialysis membrane can be measured, for example, by the same method as for the ultrafiltration membrane.
  • the material of the dialysis membrane is not particularly limited, but examples thereof include cellulose, polyacrylonitrile, polymethylmethacrylate, ethylene vinyl alcohol copolymer, polysulfone, polyamide, polyester polymer alloy and the like.
  • dialysis membrane examples include Spectra / Por (registered trademark) Float-A-Lyzer, Tube-A-Lyzer, dialysis tubing, 6dialysis tubing, and 7dialysis tubing manufactured by Spectrum Laboratories.
  • the ultrafiltration, microfiltration or dialysis membrane treatment is preferably performed at a temperature of 10 ° C or higher.
  • the temperature is more preferably 15 ° C. or higher, further preferably 20 ° C. or higher, and particularly preferably 30 ° C. or higher. By adjusting the temperature to the above range, dimers and trimers can be reduced more efficiently.
  • the temperature is preferably 90 ° C or lower, more preferably 80 ° C or lower, further preferably 70 ° C or lower, and particularly preferably 60 ° C or lower.
  • Ultrafiltration, microfiltration or dialysis membrane treatment can be performed while adding water to the crude composition or while adjusting the pH of the crude composition. Water may be added to the crude composition intermittently or continuously to the crude composition.
  • the end point of ultrafiltration, microfiltration or dialysis membrane treatment may be appropriately determined and is not limited.
  • the ultrafiltration, microfiltration or dialysis membrane treatment in order to improve the durability of the filtration membrane, it may be backwashed with water about once for a filtration time of 1 to 24 hours.
  • the polymer (I) containing substantially no dimer and trimer is usually contained.
  • An aqueous solution is obtained.
  • the polymer (I) used in the above production method may be the polymer (I) contained in the obtained aqueous solution, or the polymer (I) obtained by separating the aqueous solution from the aqueous solution.
  • the method for separating the polymer (I) from the aqueous solution is not particularly limited.
  • the polymer (I) can be separated by a method such as coagulation of the polymer (I) in an aqueous solution, washing and drying.
  • an aqueous solution containing the polymer (I) can be used as the polymer (I).
  • the preferred content of the dimer and trimer of the monomer (I) with respect to the polymer (I) in the aqueous solution is the same as the content of the dimer and trimer in the polymer (1).
  • the above-mentioned polymerization step may be a step of polymerizing tetrafluoroethylene in the presence of a nucleating agent.
  • the nucleating agent is preferably at least one selected from the group consisting of fluoropolyethers, nonionic surfactants and chain transfer agents.
  • the polymerization step is a step of obtaining PTFE by polymerizing tetrafluoroethylene (and optionally a modifying monomer) in an aqueous medium in the presence of the polymer (I) and the nucleating agent. It is preferable.
  • perfluoropolyether is preferable.
  • the fluoropolyether preferably has repeating units represented by the formulas (1a) to (1d).
  • (—CFCF 3 —CF 2 —O—) n (1a) (—CF 2 —CF 2 —CF 2 —O—) n (1b) (—CF 2 —CF 2 —O—) n — (— CF 2 —O—) m
  • (1c) (—CF 2 —CFCF 3 —O—) n — (— CF 2 —O—) m (1d)
  • m and n are integers of 1 or more.
  • fluoropolyether a fluoropolyether acid or a salt thereof is preferable, and the fluoropolyether acid is preferably a carboxylic acid, a sulfonic acid, a sulfonamide, or a phosphonic acid, and more preferably a carboxylic acid.
  • fluoropolyether acids or salts thereof fluoropolyether acid salts are preferable, fluoropolyether acid ammonium salts are more preferable, and fluoropolyethercarboxylic acid ammonium salts are further preferable.
  • the fluoropolyether acids or salts thereof can have any chain structure in which the oxygen atoms in the backbone of the molecule are separated by saturated fluorocarbon groups having 1 to 3 carbon atoms. More than one type of fluorocarbon group may be present in the molecule.
  • the fluoropolyether acid or salt thereof has the following formula: CF 3 —CF 2 —CF 2 —O (—CFCF 3 —CF 2 —O—) n CFCF 3 —COOH, CF 3 —CF 2 —CF 2 —O (—CF 2 —CF 2 —CF 2 —O— ) N —CF 2 —CF 2 COOH, or HOOC-CF 2 -O (-CF 2 -CF 2 -O-) n - (- CF 2 -O-) m CF 2 COOH (In the formula, m and n are the same as above.)
  • the compound represented by or a salt thereof is preferable.
  • fluoropolyethers can have carboxylic acid groups or salts thereof at one or both ends.
  • fluoropolyethers may have sulfonic acid or phosphonic acid groups or salts thereof at one or both ends.
  • fluoropolyethers having acid functional groups on both ends may have different groups on each end.
  • the other end of the molecule is usually perfluorinated, but may contain hydrogen or chlorine atoms.
  • Fluoropolyethers having acid groups at one or both ends have at least 2 ether oxygens, preferably at least 4 ether oxygens, and even more preferably at least 6 ether oxygens.
  • at least one of the fluorocarbon groups that dissociate the ether oxygen more preferably at least two of such fluorocarbon groups, have 2 or 3 carbon atoms.
  • at least 50% of the fluorocarbon groups that separate the ether oxygen have 2 or 3 carbon atoms.
  • the fluoropolyether has a total of at least 15 carbon atoms, eg a preferred minimum value for n or n + m in the above repeating unit structure is at least 5.
  • fluoropolyether having acid groups at one or both ends can be used in the method according to the present disclosure.
  • the fluoropolyether may contain multiple compounds at various ratios within the molecular weight range relative to the average molecular weight. ..
  • the fluoropolyether preferably has a number average molecular weight of 800 g / mol or more. Since the fluoropolyether acid or its salt may be difficult to disperse in an aqueous medium, the number average molecular weight is preferably less than 6000 g / mol.
  • the number average molecular weight of the fluoropolyether acid or its salt is more preferably 800 to 3500 g / mol, further preferably 900 to 3500 g / mol, and further preferably 1000 to 2500 g / mol.
  • the amount of the fluoropolyether is preferably 5 to 5000 mass ppm, more preferably 5 to 3000 mass ppm, still more preferably 5 to 2000 mass ppm, and still more preferably 5 to 5000 mass ppm with respect to the aqueous medium.
  • a preferable lower limit is 10 ppm, 20 mass ppm, 30 mass ppm and 50 mass ppm in a preferable order, and a further preferable upper limit is 1000 mass ppm, 500 mass ppm and 100 mass ppm in a preferable order.
  • the nonionic surfactant usually does not contain a charged group and has a hydrophobic portion which is a long chain hydrocarbon.
  • the hydrophilic portion of the nonionic surfactant contains water-soluble functional groups, such as chains of ethylene ether derived from polymerization with ethylene oxide.
  • nonionic surfactants Polyoxyethylene alkyl ether, polyoxyethylene alkylphenyl ether, polyoxyethylene alkyl ester, sorbitan alkyl ester, polyoxyethylene sorbitan alkyl ester, glycerol ester and their derivatives.
  • polyoxyethylene alkyl ethers polyoxyethylene lauryl ether, polyoxyethylene cetyl ether, polyoxyethylene stearyl ether, polyoxyethylene oleyl ether, polyoxyethylene behenyl ether and the like.
  • polyoxyethylene alkyl phenyl ethers polyoxyethylene nonyl phenyl ether, polyoxyethylene octyl phenyl ether and the like.
  • polyoxyethylene alkyl ester polyethylene glycol monolaurate, polyethylene glycol monooleate, polyethylene glycol monostearate and the like.
  • sorbitan alkyl ester polyoxyethylene sorbitan monolaurate, polyoxyethylene sorbitan monopalmitate, polyoxyethylene sorbitan monostearate, polyoxyethylene sorbitan monooleate and the like.
  • polyoxyethylene sorbitan alkyl ester polyoxyethylene sorbitan monolaurate, polyoxyethylene sorbitan monopalmitate, polyoxyethylene sorbitan monostearate and the like.
  • glycerol ester glycerol monomyristate, glycerol monostearate, glycerol monooleate and the like.
  • polyoxyethylene alkylamine polyoxyethylene alkylphenyl-formaldehyde condensate, polyoxyethylene alkyl ether phosphate and the like.
  • the ethers and esters may have an HLB value of 10-18.
  • nonionic surfactant examples include Triton (registered trademark) X series (X15, X45, X100, etc.), Tergitol (registered trademark) 15-S series, and Tergitol (registered trademark) TMN series (TMN) manufactured by Dow Chemical Company. -6, TMN-10, TMN-100, etc.), Tergitol (registered trademark) L series, Pluronic (registered trademark) R series manufactured by BASF (31R1, 17R2, 10R5, 25R4 (m-22, n-23), Examples thereof include Iconol (registered trademark) TDA series (TDA-6, TDA-9, TDA-10).
  • nonionic surfactant as the nucleating agent examples include the above-mentioned nonionic surfactants, and among them, the nonionic surfactant containing no fluorine is preferable.
  • ether type nonionic surfactants such as polyoxyethylene alkyl phenyl ether, polyoxyethylene alkyl ether and polyoxyethylene alkylene alkyl ether; polyoxyethylene derivatives such as ethylene oxide / propylene oxide block copolymers; sorbitan fatty acid Ester, polyoxyethylene sorbitan fatty acid ester, polyoxyethylene sorbitol fatty acid ester, glycerin fatty acid ester, polyoxyethylene fatty acid ester and other ester type nonionic surfactants; polyoxyethylene alkylamine, alkyl alkanolamide and other amine-based non-ionic surfactants Ionic surfactants; and the like.
  • the hydrophobic group may be any of an alkylphenol group, a linear alkyl group and a branched alkyl group.
  • nonionic surfactant examples include the following general formula (i) R 3 —OA 5 —H (i) (In the formula, R 3 is a linear or branched primary or secondary alkyl group having 8 to 18 carbon atoms, and A 5 is a polyoxyalkylene chain.) Can be mentioned.
  • the carbon number of R 3 is preferably 10 to 16, and more preferably 12 to 16.
  • the polyoxyalkylene chain may be composed of oxyethylene and oxypropylene.
  • the number of oxyethylene units can include either the broad or narrow unimodal distribution normally provided, or the broader or bimodal distribution obtained by blending.
  • the oxyethylene groups and oxypropylene groups in the polyoxyalkylene chain may be arranged in blocks or randomly.
  • a polyoxyalkylene chain composed of an average number of repeating oxyethylene groups of 7 to 12 and an average number of repeating oxypropylene groups of 0 to 2 is preferable.
  • a 1 has an oxypropylene group of 0.5 to 1.5 on average, low foaming property is good, which is preferable.
  • R 3 is more preferably (R ′) (R ′′) HC—, where R ′ and R ′′ are the same or different straight chain, branched chain or cyclic alkyl groups. And the total amount of carbon atoms is at least 5, preferably 7 to 17. Preferably, at least one of R'or R '' is a branched or cyclic hydrocarbon group.
  • nonionic surfactant examples include C 13 H 27 —O— (C 2 H 4 O) 10 —H, C 12 H 25 —O— (C 2 H 4 O) 10 —H, C 10 H 21 CH (CH 3 ) CH 2 —O— (C 2 H 4 O) 9 —H, C 13 H 27 —O— (C 2 H 4 O) 9 — (CH (CH 3 ) CH 2 O) —H, C 16 H 33 —O— (C 2 H 4 O) 10 —H, HC (C 5 H 11 ) (C 7 H 15 ) —O— (C 2 H 4 O) 9 —H and the like. Be done.
  • the nonionic surfactant may be a block copolymer of polyethylene glycol-polypropylene glycol-polyethylene glycol.
  • nonionic surfactants examples include Genapol X080 (product name, manufactured by Clariant) and Neugen TDS series (manufactured by Dai-ichi Kogyo Seiyaku Co., Ltd.) such as Neugen TDS-80 (trade name).
  • Leocall TD-90 trade name as an example Leocall TD series (made by Lion), Lionol (registered trademark) TD series (made by Lion), T-Det A138 (trade name) as an example T-Det A Examples include series (manufactured by Harcros Chemicals), Tartor (registered trademark) 15S series (manufactured by Dow Chemical).
  • Examples of commercially available products of the above polyoxyethylene alkyl ether include, for example, Genapol X080 (product name, manufactured by Clariant), Tajitol 9-S-15 (product name, manufactured by Clariant), Neugen TDS-80 (product name, first). Industrial Pharmaceutical Co., Ltd.), Leocoll TD90 (product name, manufactured by Lion), Pronon 104 (product name, manufactured by NOF CORPORATION), and the like.
  • the nonionic surfactant is an ethoxylate of 2,6,8-trimethyl-4-nonanol having an average of about 4 to about 18 ethylene oxide units, and an average of about 6 to about 12 ethylene oxide units. Also preferred is the ethoxylate of 6,8-trimethyl-4-nonanol, or a mixture thereof.
  • This type of nonionic surfactant is also commercially available, for example, as TERGITOL TMN-6, TERGITOL TMN-10, and TERGITOL TMN-100X (both product names, manufactured by Dow Chemical Co.).
  • the hydrophobic group of the nonionic surfactant may be any of an alkylphenol group, a linear alkyl group and a branched alkyl group.
  • nonionic surfactant examples include those represented by the following general formula (ii) R 4 -C 6 H 4 -OA 6 -H (ii) (In the formula, R 4 is a linear or branched primary or secondary alkyl group having 4 to 12 carbon atoms, and A 6 is a polyoxyalkylene chain.) An ionic surfactant is mentioned.
  • polyoxyethylene alkylphenyl ether-based nonionic compound examples include Triton X-100 (trade name, manufactured by Dow Chemical Co.).
  • nonionic surfactant also include polyol compounds. Specific examples thereof include those described in International Publication No. 2011/014715.
  • Typical examples of the polyol compound include compounds having one or more sugar units as the polyol unit. The sugar unit may be modified to contain at least one long chain. Suitable polyol compounds containing at least one long chain moiety include, for example, alkyl glycosides, modified alkyl glycosides, sugar esters, and combinations thereof.
  • Sugars include, but are not limited to, monosaccharides, oligosaccharides, and sorbitan. Monosaccharides include pentoses and hexoses.
  • Typical examples of monosaccharides include ribose, glucose, galactose, mannose, fructose, arabinose and xylose.
  • Oligosaccharides include oligomers of 2-10 identical or different monosaccharides. Examples of oligosaccharides include, but are not limited to, saccharose, maltose, lactose, raffinose, and isomaltose.
  • sugars suitable for use as the polyol compound include a five membered ring of four carbon atoms and one heteroatom (typically oxygen or sulfur, but preferably an oxygen atom). Or a cyclic compound containing a 6-membered ring of 5 carbon atoms and one hetero atom as described above, preferably an oxygen atom. They further contain at least 2 or at least 3 hydroxy groups (—OH groups) attached to carbon ring atoms.
  • the sugar is the hydrogen atom of a hydroxy group (and / or hydroxyalkyl group) attached to a carbon ring atom, such that an ether or ester bond is created between the long chain residue and the sugar moiety. One or more of these are modified in that they are replaced by long chain residues.
  • the sugar-based polyol may contain one sugar unit or a plurality of sugar units.
  • the sugar unit or sugar units may be modified with long chain moieties as described above.
  • Specific examples of sugar-based polyol compounds include glycosides, sugar esters, sorbitan esters, and mixtures and combinations thereof.
  • a preferred class of polyol compounds are alkyl or modified alkyl glucosides. These types of surfactants contain at least one glucose moiety. (Wherein x represents 0, 1, 2, 3, 4, or 5 and R 1 and R 2 independently represent H or a long chain unit containing at least 6 carbon atoms. Provided that at least one of R 1 and R 2 is not H). Typical examples of R 1 and R 2 include aliphatic alcohol residues.
  • aliphatic alcohols examples include hexanol, heptanol, octanol, nonanol, decanol, undecanol, dodecanol (lauryl alcohol), tetradecanol, hexadecanol (cetyl alcohol), heptadecanol, octadecanol (stearyl alcohol), Eicosanoic acid, and combinations thereof.
  • the above formula represents a specific example of an alkyl polyglucoside representing a pyranose form of glucose, other sugars or sugars of the same sugar but different enantiomers or diastereomeric forms may be used. To be understood.
  • Alkyl glucosides are available, for example, by acid-catalyzed reactions of glucose, starch, or n-butyl glucosides with aliphatic alcohols, which typically yield a mixture of different alkyl glucosides (Alkylpolyglycylside, Romppp. , Lexikon Chemie, Version 2.0, Stuttgart / New York, Georg Thieme Verlag, 1999).
  • aliphatic alcohols examples include hexanol, heptanol, octanol, nonanol, decanol, undecanol, dodecanol (lauryl alcohol), tetradecanol, hexadecanol (cetyl alcohol), heptadecanol, octadecanol (stearyl alcohol), Eicosanoic acid, and combinations thereof.
  • Alkyl glucosides are also commercially available under the trade name GLUCOPON or DISPONIL from Cognis GmbH, Dusseldorf, Germany.
  • nonionic surfactants include bifunctional block copolymers supplied by BASF as Pluronic® R series and tridecyl alcohol alkoxylates supplied by BASF as Iconol® TDA series. Be done.
  • the nonionic surfactant is selected from the group consisting of a nonionic surfactant represented by the general formula (i) and a nonionic surfactant represented by the general formula (ii). At least one type is preferable.
  • the amount of the nonionic surfactant is preferably 0.1 to 0.0000001 mass% with respect to the aqueous medium.
  • the lower limit of the amount of the nonionic surfactant is 0.000001% by mass, 0.000005% by mass, and 0.00001% by mass in a preferable order.
  • the upper limit of the amount of the nonionic surfactant is 0.01% by mass, 0.005% by mass, 0.001% by mass, 0.0005% by mass, and 0.0001% by mass in a preferable order.
  • the chain transfer agent described below can also be used.
  • the chain transfer agent used as the nucleating agent is preferably at least one selected from the group consisting of alkanes and alcohols from the viewpoint of polymerization reactivity, crosslinking reactivity, availability, and the like.
  • the alkane preferably has 1 to 6 carbon atoms, more preferably 2 to 4 carbon atoms, and even more preferably 3 to 4 carbon atoms.
  • the carbon number of the alcohol is preferably 1-5, more preferably 1-4, and even more preferably 3-4.
  • the chain transfer agent is preferably at least one selected from the group consisting of alcohols having 1 to 4 carbon atoms and alkanes having 2 to 4 carbon atoms, and selected from the group consisting of isopropanol, sec-butanol and tert-butanol. At least one kind is more preferable. In particular, by using a chain transfer agent containing tertiary carbon, more particles can be generated during polymerization.
  • a chain transfer agent is preferable, and a chain transfer agent and one or both of a nonionic surfactant and a fluoropolyether are more preferable.
  • the nucleating agent includes a combination of the chain transfer agent and the nonionic surfactant, a chain transfer agent. Combinations of agents and fluoropolyethers, chain transfer agents, nonionic surfactants and fluoropolyethers are included. Among them, a combination of a chain transfer agent and a nonionic surfactant is preferable as the nucleating agent.
  • the amount of the nucleating agent to be added can generate more particles during the polymerization, and further, since the average primary particle diameter and the primary particles having a smaller aspect ratio can be obtained, relative to the aqueous medium, It is preferably 0.001 to 0.1 mass ppm.
  • the lower limit of the amount of the nucleating agent is 0.01 mass ppm, 0.05 mass ppm, and 0.1 mass ppm in the preferred order.
  • the upper limit of the amount of the nucleating agent is 2000 mass ppm, 1000 mass ppm, 500 mass ppm, 100 mass ppm, 50 mass ppm, and 10 mass ppm in the order of preference.
  • the mass ratio of the chain transfer agent and the nonionic surfactant is Since more particles can be generated, and further, primary particles having a smaller average primary particle diameter and aspect ratio are obtained, it is preferably 1000/1 to 1/5, more preferably 200 / It is 1 to 1/2, 100/1 to 1/1, and more preferably 50/1 to 2/1.
  • the nucleating agent is added to the aqueous medium before the polymerization reaction is started or before the concentration of PTFE in the aqueous dispersion reaches 5.0% by mass as the polymerization reaction proceeds.
  • a nucleating agent at the initial stage of polymerization, more particles can be generated during polymerization, and further, primary particles having a smaller average primary particle diameter and smaller aspect ratio can be obtained. That is, the nucleating agent may be added before the initiation of the polymerization, may be added at the same time as the initiation of the polymerization, or may be added during the period when the nuclei of the PTFE particles are formed after the initiation of the polymerization. ..
  • the time for adding the nucleating agent is before the initiation of the polymerization or before the concentration of PTFE in the aqueous dispersion reaches 5.0% by mass due to the progress of the polymerization reaction, and preferably before the initiation of the polymerization or the concentration of PTFE. Before the start of polymerization or before the concentration of PTFE reaches 1.0% by mass, more preferably before the start of polymerization or the concentration of PTFE is 0.5% by mass. Before, particularly preferably before or at the same time as the initiation of polymerization.
  • the amount of the nucleating agent to be added allows more particles to be generated during the polymerization, and further, the average primary particle diameter and the primary particles having a smaller aspect ratio can be obtained, so that the obtained PTFE can be used.
  • the lower limit of the amount of the nucleating agent is 0.01 mass ppm, 0.05 mass ppm, and 0.1 mass ppm in the preferred order.
  • the upper limit of the amount of the nucleating agent is 2000 mass ppm, 1000 mass ppm, 500 mass ppm, 100 mass ppm, 50 mass ppm, and 10 mass ppm in the order of preference.
  • the above-mentioned polymerization step may be a step of polymerizing tetrafluoroethylene in the presence of a chain transfer agent.
  • the chain transfer agent include esters such as dimethyl malonate, diethyl malonate, methyl acetate, ethyl acetate, butyl acetate and dimethyl succinate, as well as isopentane, methane, ethane, propane, isobutane, methanol, ethanol and isopropanol. , Acetone, various mercaptans, various halogenated hydrocarbons such as carbon tetrachloride, and cyclohexane.
  • Examples of the polymerization method using a bromine compound or iodine compound include a method of polymerizing a fluoromonomer in an aqueous medium in the presence of a bromine compound or iodine compound in a substantially oxygen-free state ( Iodine transfer polymerization method).
  • Typical examples of the bromine compound or iodine compound used include, for example, the general formula: R a I x Br y (In the formula, x and y are each an integer of 0 to 2 and satisfy 1 ⁇ x + y ⁇ 2, and R a is a saturated or unsaturated fluorohydrocarbon group having 1 to 16 carbon atoms or chlorofluoro. And a compound represented by a hydrocarbon group or a hydrocarbon group having 1 to 3 carbon atoms, which may contain an oxygen atom).
  • a bromine compound or an iodine compound iodine or bromine is introduced into the polymer and functions as a crosslinking point.
  • bromine compound or iodine compound examples include 1,3-diiodoperfluoropropane, 2-iodoperfluoropropane, 1,3-diiodo-2-chloroperfluoropropane, 1,4-diiodoperfluorobutane, 1 , 5-diiodo-2,4-dichloroperfluoropentane, 1,6-diiodoperfluorohexane, 1,8-diiodoperfluorooctane, 1,12-diiodoperfluorododecane, 1,16-diiodine perfluoro hexadecane, diiodomethane, 1,2-diiodoethane, 1,3-diiodo -n- propane, CF 2 Br 2, BrCF 2 CF 2 Br, CF 3 CFBrCF 2 Br, CFClBr 2, BrCF 2 CFCl
  • alkanes and alcohols are preferable as the chain transfer agent from the viewpoints of polymerization reactivity, crosslinking reactivity, availability, and the like.
  • the alkane preferably has 1 to 6 carbon atoms, more preferably has 1 to 5 carbon atoms, further preferably has 2 to 4 carbon atoms, and particularly preferably has 3 to 4 carbon atoms.
  • the alcohol preferably has 1 to 5 carbon atoms, more preferably 1 to 4 carbon atoms, and further preferably 3 to 4 carbon atoms.
  • the chain transfer agent is preferably at least one selected from the group consisting of alcohols having 1 to 4 carbon atoms and alkanes having 2 to 4 carbon atoms, and particularly, methane, ethane, propane, isobutane, methanol, ethanol, and At least one selected from the group consisting of isopropanol is preferable.
  • the amount of the chain transfer agent is preferably 0.001 to 10000 mass ppm with respect to the aqueous medium.
  • the amount of the chain transfer agent is more preferably 0.01 mass ppm or more, further preferably 0.05 mass ppm or more, particularly preferably 0.1 mass ppm or more, particularly preferably 0.5 mass ppm or more with respect to the aqueous medium. Particularly preferred.
  • the amount of the chain transfer agent is more preferably 1000 mass ppm or less, further preferably 500 mass ppm or less, particularly preferably 100 mass ppm or less, particularly preferably 10 mass ppm or less, based on the aqueous medium. ..
  • the chain transfer agent may be added to the reaction vessel all at once before the start of polymerization, may be added all at once after the start of polymerization, or may be added in multiple portions during polymerization. Alternatively, it may be added continuously during the polymerization.
  • additives can be used for stabilizing each compound.
  • examples of the additive include a buffer, a pH adjuster, a stabilizing aid, and a dispersion stabilizer.
  • paraffin wax paraffin wax, fluorine-based oil, fluorine-based solvent, silicone oil and the like are preferable.
  • the stabilizing aids may be used alone or in combination of two or more. Paraffin wax is more preferable as the stabilizing aid.
  • the paraffin wax may be liquid, semi-solid or solid at room temperature, but saturated hydrocarbon having 12 or more carbon atoms is preferable.
  • the melting point of paraffin wax is usually preferably 40 to 65 ° C, more preferably 50 to 65 ° C.
  • the amount of the stabilizing aid used is preferably 0.1 to 12% by mass, and more preferably 0.1 to 8% by mass, based on the mass of the aqueous medium used. It is desirable that the stabilizing aid is sufficiently hydrophobic so that it is not completely separated from the PTFE dispersion after the PTFE polymerization and becomes a contaminant component. Further, the stabilizing aid is preferably removed from the aqueous dispersion obtained by the polymerization.
  • pH adjusters include ammonia, sodium hydroxide, potassium hydroxide, sodium carbonate, potassium carbonate, ammonium carbonate, sodium hydrogen carbonate, potassium hydrogen carbonate, ammonium hydrogen carbonate, sodium phosphate, potassium phosphate, sodium citrate, and citric acid. Potassium acid, ammonium citrate, sodium gluconate, potassium gluconate, ammonium gluconate and the like can be used.
  • the pH can be measured with a pH meter manufactured by orion.
  • the pH of the aqueous medium when polymerizing TFE is preferably basic.
  • the pH of the aqueous medium may be adjusted by adding a pH adjuster to the aqueous medium.
  • the pH of the aqueous medium at the time of polymerizing TFE is preferably 7.1 or higher, more preferably 7.5 or higher.
  • the polymerization is carried out by charging the polymerization reactor with an aqueous medium, the above-mentioned polymer (I), tetrafluoroethylene, a modified monomer optionally added, and optionally other additives.
  • an aqueous medium By stirring the contents and maintaining the reactor at a predetermined polymerization temperature, and then adding a predetermined amount of a polymerization initiator to start the polymerization reaction.
  • a monomer, a polymerization initiator, a chain transfer agent, the above polymer (I) and the like may be additionally added depending on the purpose.
  • the polymer (I) may be added after the polymerization reaction has started.
  • the polymerization initiator is not particularly limited as long as it can generate radicals in the polymerization temperature range, and known oil-soluble and / or water-soluble polymerization initiators can be used. Furthermore, the polymerization can be initiated as a redox in combination with a reducing agent or the like. The concentration of the polymerization initiator is appropriately determined depending on the type of monomer, the molecular weight of the target fluoropolymer, and the reaction rate.
  • an oil-soluble radical polymerization initiator or a water-soluble radical polymerization initiator can be used as the above-mentioned polymerization initiator.
  • the oil-soluble radical polymerization initiator may be a known oil-soluble peroxide, for example, dialkyl peroxycarbonates such as diisopropyl peroxydicarbonate and disec-butyl peroxydicarbonate, t-butyl peroxycarbonate.
  • dialkyl peroxycarbonates such as diisopropyl peroxydicarbonate and disec-butyl peroxydicarbonate, t-butyl peroxycarbonate.
  • Peroxyesters such as isobutyrate and t-butylperoxypivalate, dialkylperoxides such as dit-butylperoxide, and the like, di ( ⁇ -hydro-dodecafluoroheptanoyl) peroxide and di ( ⁇ -Hydro-tetradecafluoroheptanoyl) peroxide, di ( ⁇ -hydro-hexadecafluorononanoyl) peroxide, di (perfluorobutyryl) peroxide, di (perfluorovaleryl) peroxide, di (Perfluorohexanoyl) peroxide, di (perfluoroheptanoyl) peroxide, di (perfluorooctanoyl) peroxide, di (perfluorononanoyl) peroxide, di ( ⁇ -chloro-hexafluorobutyryl) Peroxide, di ( ⁇ -chloro-decafluor
  • the water-soluble radical polymerization initiator may be a known water-soluble peroxide, and examples thereof include ammonium salts such as persulfuric acid, perboric acid, perchloric acid, perphosphoric acid and percarbonic acid, potassium salts and sodium salts. , Organic peroxides such as disuccinic acid peroxide and diglutaric acid peroxide, t-butyl permaleate, and t-butyl hydroperoxide. A reducing agent such as sulfites and sulfites may also be included, and the amount thereof may be 0.1 to 20 times that of the peroxide.
  • a redox initiator in which an oxidizing agent and a reducing agent are combined as a polymerization initiator.
  • the oxidizing agent include persulfates, organic peroxides, potassium permanganate, manganese triacetate, ammonium cerium nitrate, and bromates.
  • the reducing agent include sulfite, bisulfite, bromate, diimine, oxalic acid and the like.
  • the persulfate include ammonium persulfate and potassium persulfate.
  • Examples of the sulfite include sodium sulfite and ammonium sulfite.
  • a copper salt and an iron salt to the combination of redox initiators.
  • Examples of the copper salt include copper (II) sulfate, and examples of the iron salt include iron (II) sulfate.
  • redox initiators examples include potassium permanganate / oxalic acid, ammonium persulfate / bisulfite / iron (II) sulfate, ammonium persulfate / sulfite / iron (II) sulfate, ammonium persulfate / sulfite, ammonium persulfate.
  • potassium permanganate / oxalic acid, ammonium persulfate / Sulfite / iron (II) sulfate is preferred.
  • a redox initiator either the oxidizing agent or the reducing agent may be charged into the polymerization tank in advance, and then the other may be continuously or intermittently added to initiate the polymerization.
  • potassium permanganate / oxalic acid it is preferable to charge oxalic acid into a polymerization tank and continuously add potassium permanganate thereto.
  • the addition amount of the polymerization initiator is not particularly limited, but an amount not exceeding a marked decrease in the polymerization rate (for example, several ppm vs. water concentration) is added in batch at the beginning of the polymerization, or sequentially or continuously. It may be added.
  • the upper limit is a range in which the reaction temperature may be increased while the heat of the polymerization reaction is removed from the device side, and the more preferable upper limit is a range in which the heat of the polymerization reaction can be removed from the device side.
  • a decomposing agent or the like may be further added to adjust the polymerization rate and the molecular weight depending on the purpose.
  • TFE may be polymerized in the presence of an anionic hydrocarbon surfactant.
  • anionic hydrocarbon surfactant By using the anionic hydrocarbon surfactant, the stability of the aqueous dispersion produced by the polymerization is improved, and the TFE polymerization proceeds smoothly.
  • TFE may be polymerized in the substantial absence of an anionic hydrocarbon surfactant.
  • the TFE polymerization proceeds smoothly without using an anionic hydrocarbon surfactant.
  • substantially in the absence of anionic hydrocarbon-based surfactant means that the amount of the anionic hydrocarbon-based surfactant is 10 mass ppm or less with respect to the aqueous medium, and preferably Is 1 mass ppm or less, more preferably 100 mass ppb or less, still more preferably 10 mass ppb or less, still more preferably 1 mass ppb or less.
  • the anionic hydrocarbon-based surfactant usually has a hydrophilic portion such as carboxylate, sulfonate or sulfate and a hydrophobic portion which is a long chain hydrocarbon portion such as alkyl.
  • anionic hydrocarbon-based surfactant examples include Versatic (registered trademark) 10 of Resolution Performance Products, and Avance S series (S-70, S-74, etc.) manufactured by BASF.
  • anionic hydrocarbon-based surfactant examples include RLM (wherein R is a linear or branched alkyl group having 1 or more carbon atoms which may have a substituent, or a substituted group). It is a cyclic alkyl group having 3 or more carbon atoms which may have a group, and when it has 3 or more carbon atoms, it may contain a monovalent or divalent heterocycle, or may form a ring.
  • RLM wherein R is a linear or branched alkyl group having 1 or more carbon atoms which may have a substituent, or a substituted group. It is a cyclic alkyl group having 3 or more carbon atoms which may have a group, and when it has 3 or more carbon atoms, it may contain a monovalent or divalent heterocycle, or may form a ring.
  • L is, -ArSO 3 -, -SO 3 - , -SO 4 -, - PO 3 - or COO - and is, M is, H, a metal atom, NR 5 4, which may have a substituent imidazo Lithium, optionally substituted pyridinium or optionally substituted phosphonium, R 5 is H or an organic group, and —ArSO 3 — is an aryl sulfonate.) Also included are anionic surfactants.
  • CH 3- (CH 2 ) n -LM as represented by lauric acid and lauryl sulfate (wherein n is an integer of 6 to 17; The same).
  • a mixture of R is an alkyl group having 12 to 16 carbon atoms and LM is a sulfate or sodium dodecyl sulfate (SDS) can also be used.
  • R 6 is a linear or branched chain having 1 or more carbon atoms which may have a substituent. Or an cyclic alkylene group having 3 or more carbon atoms which may have a substituent, and when the number of carbon atoms is 3 or more, it may include a monovalent or divalent heterocycle, or forming a good .L even if it, -ArSO 3 -, -SO 3 - , -SO 4 -, - PO 3 - or COO - and is, M is, H, a metal atom, NR 5 4, substituents Imidazolium which may have, pyridinium which may have a substituent or phosphonium which may have a substituent, R 5 is H or an organic group, —ArSO 3 — is an aryl sulfonate
  • the anionic surfactant represented by the formula (1) is also included.
  • anionic hydrocarbon-based surfactant examples include R 7 (-LM) 3 (in the formula, R 7 is a linear or branched chain having 1 or more carbon atoms which may have a substituent). Or a cyclic alkylidyne group having 3 or more carbon atoms which may have a substituent, and when it has 3 or more carbon atoms, it may include a monovalent or divalent heterocycle, forming a good .L even if it, -ArSO 3 -, -SO 3 - , -SO 4 -, - PO 3 - or COO - and is, M is, H, a metal atom, NR 5 4, substituents Imidazolium which may have, pyridinium which may have a substituent or phosphonium which may have a substituent, R 5 is H or an organic group, —ArSO 3 — is an arylsulfonic acid Anionic surfactants represented by (salts) are also included.
  • examples of the anionic hydrocarbon-based surfactant also include siloxane hydrocarbon-based surfactants.
  • examples of the siloxane hydrocarbon surfactant include Silicone Surfactants, R .; M. Hill, Marcel Dekker, Inc. , ISBN: 0-8247-00104.
  • the structure of siloxane hydrocarbon-based surfactants includes well-defined hydrophobic and hydrophilic moieties.
  • the hydrophobic portion comprises one or more dihydrocarbyl siloxane units, where the substituents on the silicone atom are wholly hydrocarbon.
  • siloxane surfactants can also be considered hydrocarbon interfacial surfactants in the sense that the carbon atoms of the hydrocarbyl group can be completely replaced by hydrogen atoms when they can be replaced by halogens such as fluorine. That is, the monovalent substituent on the carbon atom of the hydrocarbyl group is hydrogen.
  • the hydrophilic portion of the siloxane hydrocarbon surfactant is sulfate, sulfonate, phosphonate, phosphate ester, carboxylate, carbonate, sulfosuccinate, taurate (as free acid, salt or ester), phosphine oxide, betaine, betaine. It may also include one or more polar moieties containing ionic groups such as copolyols, quaternary ammonium salts and the like. The ionic hydrophobic portion may also include ionically functionalized siloxane grafts.
  • siloxane hydrocarbon surfactants examples include polydimethylsiloxane-graft- (meth) acrylic acid salts, polydimethylsiloxane-graft-polyacrylate salts and polydimethylsiloxane-grafted quaternary amines. ..
  • the polar portion of the hydrophilic portion of the siloxane hydrocarbon surfactant is polyethylene oxide (PEO), and mixed polyethers such as polyethylene oxide / propylene oxide polyether (PEO / PPO); monosaccharides and disaccharides; and It may include nonionic groups formed by water-soluble heterocycles such as pyrrolidinone.
  • the ratio of ethylene oxide to propylene oxide (EO / PO) can be varied in the mixed polyethylene oxide / propylene oxide polyether.
  • the hydrophilic portion of the siloxane hydrocarbon-based surfactant may also include a combination of ionic and nonionic moieties.
  • Such moieties include, for example, ionically end-functionalized or randomly functionalized polyethers or polyols.
  • Preferred is a siloxane having a nonionic portion, that is, a nonionic siloxane surfactant.
  • the arrangement of the hydrophobic and hydrophilic moieties of the structure of the siloxane hydrocarbon surfactant is determined by the diblock polymer (AB), triblock polymer (ABA) (where "B” represents the siloxane moiety of the molecule), Alternatively, it may take the form of a multi-block polymer. Alternatively, the siloxane surfactant may include a graft polymer.
  • Siloxane hydrocarbon surfactants are also disclosed in US Pat. No. 6,841,616.
  • siloxane-based anionic hydrocarbon surfactant examples include Lubrizol Advanced Materials, Inc. From Noveon® Consumer Specialties, Inc., SilSense TM PE-100 silicone, SilSense TM CA-1 silicone, and the like.
  • anionic hydrocarbon-based surfactant examples include Akzo Nobel Surface Chemistry LLC sulfosuccinate surfactant Lankropol (registered trademark) K8300.
  • sulfosuccinate surfactant examples include diisodecyl Na salt of sulfosuccinate, (Emulsogen (registered trademark) SB10 of Clariant), diisotridecyl Na salt of sulfosuccinate (Polyrol (registered trademark) TR / LNA of Cesapinia Chemicals) and the like.
  • anionic hydrocarbon surfactant examples include Omniva Solutions, Inc. PolyFox® surfactants such as PolyFox TM PF-156A and PolyFox TM PF-136A are also listed.
  • anionic hydrocarbon surfactant examples include, for example, the general formula ( ⁇ ): R 10 -COOM ( ⁇ ) (Wherein, R 10 is a is .M monovalent organic group containing 1 or more carbon atoms, H, a metal atom, NR 11 4, good imidazolium be substituted, substituted Which is a pyridinium which may have a group or a phosphonium which may have a substituent, and R 11 is H or an organic group, which may be the same or different. Can be mentioned. R 11 is preferably an H or C 1-10 organic group, more preferably an H or C 1-4 organic group. From the viewpoint of surface activity, the carbon number of R 10 is preferably 2 or more, and more preferably 3 or more.
  • the carbon number of R 10 is preferably 29 or less, more preferably 23 or less.
  • the metal atom of M include an alkali metal (group 1) and an alkaline earth metal (group 2), and Na, K or Li is preferable.
  • M H, a metal atom or NR 11 4 is preferable, H, an alkali metal (group 1), an alkaline earth metal (group 2) or NR 11 4 is more preferable, and H, Na, K, Li or NH 4 is used. Is more preferred, Na, K or NH 4 is even more preferred, Na or NH 4 is particularly preferred, and NH 4 is most preferred.
  • Examples of the compound ( ⁇ ) include R 12 —COOM (in the formula, R 12 is a linear or branched alkyl group, alkenyl group, alkylene group or alkenylene having 1 or more carbon atoms which may have a substituent).
  • a monovalent or divalent heterocycle may be included, or a ring may be formed, and M is the same as described above. Specific examples thereof include those represented by CH 3 — (CH 2 ) n —COOM (wherein n is an integer of 2 to 28. M is the same as above).
  • the compound ( ⁇ ) may not contain a carbonyl group (excluding the carbonyl group in the carboxyl group) from the viewpoint of emulsion stability.
  • Examples of the carbonyl group-free hydrocarbon-containing surfactant include the following formula (A): R—COO—M (A) (wherein R is an alkyl group containing 6 to 17 carbon atoms).
  • M has H, a metal atom, NR 11 4, good imidazolium be substituted, the substituent Preferred examples thereof include pyridinium which may be present, or phosphonium which may have a substituent, and R 11 is the same or different and is H or an organic group having 1 to 10 carbon atoms.
  • R is preferably an alkyl group or an alkenyl group (these may include an ether group).
  • the alkyl group or alkenyl group in R may be linear or branched. Although the carbon number of R is not limited, it is, for example, 2 to 29.
  • the carbon number of R is preferably 3 to 29, more preferably 5 to 23.
  • the carbon number of R is preferably 5 to 35, more preferably 11 to 23.
  • the carbon number of R is preferably 2 to 29, more preferably 9 to 23.
  • the carbon number of R is preferably 2 to 29, more preferably 9 to 23.
  • alkyl group and alkenyl group examples include a methyl group, an ethyl group, an isobutyl group, a t-butyl group, a vinyl group and the like.
  • anionic hydrocarbon-based surfactant also include carboxylic acid-type hydrocarbon-based surfactants.
  • carboxylic acid type hydrocarbon surfactant include butyric acid, valeric acid, caproic acid, enanthic acid, caprylic acid, pelargonic acid, capric acid, lauric acid, myristic acid, pentadecylic acid, palmitic acid, palmitoleic acid, Margaric acid, stearic acid, oleic acid, vaccenic acid, linoleic acid, (9,12,15) -linolenic acid, (6,9,12) linolenic acid, eleostearic acid, arachidic acid, 8,11-eicosadienoic acid , Mead acid, arachidonic acid, behenic acid, lignoceric acid, nervonic acid, cerotic acid, montanic acid, melissic acid, crotonic acid, myristoleic acid, palm
  • the metal atom of the formula M hydrogen of the carboxyl groups mentioned above, NR 11 4, which may imidazolium substituted, pyridinium which may have a substituent, or a substituent Examples thereof include phosphonium which may be contained, but are not particularly limited.
  • the anionic hydrocarbon-based surfactant for example, the anionic hydrocarbon-based surfactants described in WO 2013/146950 and WO 2013/1466947 can be used.
  • examples thereof include those having a saturated or unsaturated aliphatic chain having 6 to 40 carbon atoms, preferably 8 to 20 carbon atoms, and more preferably 9 to 13 carbon atoms.
  • the saturated or unsaturated aliphatic chain may be linear or branched, and may have a cyclic structure.
  • the hydrocarbon may be aromatic or may have an aromatic group.
  • the hydrocarbon may have a hetero atom such as oxygen, nitrogen or sulfur.
  • anionic hydrocarbon-based surfactant examples include alkyl sulfonate, alkyl sulfate, alkyl aryl sulfate and salts thereof; aliphatic (carboxylic) acid and salts thereof; phosphoric acid alkyl ester, phosphoric acid alkyl aryl ester or salts thereof; Among them, alkyl sulfonates, alkyl sulfates, aliphatic carboxylic acids or salts thereof are preferable.
  • alkyl sulfate or its salt ammonium lauryl sulfate and sodium lauryl sulfate are preferable.
  • aliphatic carboxylic acid or salt thereof succinic acid, decanoic acid, undecanoic acid, undecenoic acid, lauric acid, hydrododecanoic acid, or salts thereof are preferable.
  • TFE can be polymerized in the presence of a fluorine-containing surfactant (excluding compounds having a functional group capable of reacting by radical polymerization and a hydrophilic group).
  • a fluorine-containing surfactant excluding compounds having a functional group capable of reacting by radical polymerization and a hydrophilic group.
  • TFE substantially in the absence of a fluorine-containing surfactant (excluding compounds having a functional group capable of reacting by radical polymerization and a hydrophilic group).
  • a fluorine-containing surfactant excluding compounds having a functional group capable of reacting by radical polymerization and a hydrophilic group.
  • the TFE polymerization proceeds smoothly without using a fluorine-containing surfactant.
  • a composition substantially free of a fluorinated surfactant can be easily obtained.
  • substantially in the absence of a fluorine-containing surfactant means that the content of the fluorine-containing surfactant in the aqueous medium is 10 mass ppm or less, preferably 1 mass ppm or less. Yes, more preferably 100 mass ppb or less, still more preferably 10 mass ppb or less, still more preferably 1 mass ppb or less.
  • fluorine-containing surfactant examples include those described above as the fluorine-containing surfactant which is preferably substantially not contained in the composition of the present disclosure.
  • the amount of adhesion is preferably 3.0% by mass or less, more preferably 2.0% by mass or less, more preferably 1.0% by mass or less, with respect to the finally obtained PTFE.
  • 0.8 mass% or less is more preferable, 0.7 mass% or less is still more preferable, and 0.6 mass% or less is particularly preferable.
  • an aqueous dispersion containing polytetrafluoroethylene and the polymer (I) is obtained.
  • the composition of the present disclosure further comprises a step of recovering the PTFE aqueous dispersion obtained by the above method, A step of aggregating PTFE in the aqueous PTFE dispersion, A step of collecting the agglomerated PTFE, and A step of drying the collected PTFE at 100 to 300 ° C., Among them, it can be suitably obtained by a manufacturing method including at least one step.
  • a powder can be produced by aggregating the PTFE contained in the above aqueous dispersion.
  • the composition of the present disclosure may be a powder.
  • the aqueous dispersion containing PTFE and the polymer (I) may be subjected to post-treatment such as concentration, if necessary, and then subjected to coagulation, washing and drying to be used as a powder for various purposes.
  • post-treatment such as concentration, if necessary
  • the aqueous dispersion obtained by polymerization of polymer latex or the like is usually used in water to obtain a polymer concentration of 10 to 25% by mass (preferably 10 to 20% by mass).
  • the aggregation may be performed while adding a water-soluble organic compound such as methanol or acetone, an inorganic salt such as potassium nitrate or ammonium carbonate, or an inorganic acid such as hydrochloric acid, sulfuric acid or nitric acid as a coagulant.
  • the agglomeration may be continuously performed using an in-line mixer or the like.
  • the composition of the pigmented or filler-containing powder in which the pigments and fillers are uniformly mixed You can get things.
  • the wet powder obtained by coagulating the PTFE and the polymer (I) is usually dried by a means such as vacuum, high frequency wave, hot air, etc., while keeping the wet powder not to flow so much, preferably in a stationary state.
  • Friction between powders, especially at high temperatures, generally has an unfavorable effect on fine powder type PTFE. This is because particles of this kind of PTFE have the property of easily fibrillating even with a small shearing force and losing the original stable particle structure state.
  • the drying can be performed at a drying temperature of 10 to 300 ° C. (preferably 10 to 250 ° C.), preferably 100 to 300 (preferably 100 to 250 ° C.).
  • the powder preferably has an average particle size (average secondary particle size) of 100 to 2000 ⁇ m.
  • the lower limit of the average secondary particle diameter is more preferably 200 ⁇ m or more, further preferably 300 ⁇ m or more.
  • the upper limit of the average secondary particle diameter is preferably 1000 ⁇ m or less, more preferably 800 ⁇ m or less, and particularly preferably 700 ⁇ m or less.
  • the average particle diameter is a value measured according to JIS K6891.
  • the composition of the present disclosure when the composition of the present disclosure is a powder, the composition of the present disclosure preferably has a total amount of the polymer (I) and polytetrafluoroethylene of 90% by mass or more, and preferably 99% by mass or more. More preferably, it is substantially 100% by mass.
  • the composition of the present disclosure has stretchability and non-melt processability, and is useful as a raw material for a stretched body (porous body).
  • a stretched product excellent in breaking strength and stress relaxation time can be obtained.
  • a powder of the composition of the present disclosure mixed with an extrusion aid can be paste extruded, if necessary, rolled to remove the extrusion aid by drying, and then stretched in at least one direction to obtain a stretched body. ..
  • the composition of the present disclosure easily fibrillates PTFE, and becomes a stretched body composed of knots and fibers. This stretched body is also a porous body having a high porosity.
  • the present disclosure also relates to a stretched body comprising the composition described above.
  • the stretched body of the present disclosure is obtained by subjecting the above composition to paste extrusion rolling, followed by unsintering or semi-sintering, stretching in at least one direction (preferably roll stretching in the rolling direction, and then stretching in the width direction by a tenter). ), Can be manufactured.
  • the stretched product of the present disclosure may be a uniaxially stretched film obtained by roll-stretching the extrudate, or a biaxially stretched film obtained by stretching the uniaxially stretched film in the width direction using a tenter or the like. It may be a membrane.
  • the extrudate may be subjected to a semi-firing treatment prior to stretching.
  • the stretched product of the present disclosure may contain only PTFE and the polymer (I), or may contain PTFE, the polymer (I) and the above-mentioned pigments and fillers. And a polymer (I) alone.
  • the stretched body of the present disclosure preferably has a porosity in the range of 30% to 99%.
  • the porosity is more preferably 40% or more, further preferably 50% or more, further preferably 60% or more, particularly preferably 70% or more. If the proportion of PTFE in the stretched body is too small, the strength of the stretched body may be insufficient, so the porosity is preferably 95% or less, more preferably 90% or less.
  • the density ⁇ of the stretched body is obtained by measuring the mass of the sample cut into a certain length with a precision balance, and measuring the mass and outer diameter of the sample by the following formula. Calculate the density.
  • ⁇ M / (r ⁇ r ⁇ ⁇ ) ⁇ L
  • ⁇ density (g / cm 3 )
  • M mass (g)
  • r radius (cm)
  • L length (cm)
  • ⁇ circumferential ratio
  • the outer diameter of the stretched body is measured using a laser displacement sensor. The radius is the value obtained by dividing the value by 2. The above measurement and calculation are performed at three points, and the average value thereof is taken as the density.
  • the present disclosure further includes polytetrafluoroethylene and a polymer (I) containing a polymerized unit (I) based on a monomer represented by the following general formula (I), wherein the breaking strength A is 10.0 N or more.
  • X 1 and X 3 are each independently F, Cl, H or CF 3 ;
  • a 0 is an anionic group;
  • X 2 is H, F, an alkyl group or a fluorine-containing group.
  • R is a linking group;
  • Z 1 and Z 2 are each independently H, F, an alkyl group or a fluorine-containing alkyl group;
  • m is an integer of 1 or more.
  • the polytetrafluoroethylene and the polymer (I) are the same as those described for the composition of the present disclosure, and each can adopt a suitable aspect.
  • the stretched product of the present disclosure has a breaking strength A of preferably 13.0 N or more, more preferably 16.0 N or more, still more preferably 19.0 N or more.
  • Break strength of the stretched body The stretched body is sandwiched and fixed by movable jaws having a gauge length of 5.0 cm, and a tensile test is performed at 25 ° C at a speed of 300 mm / min. ..
  • the stretched body of the present disclosure preferably has a stress relaxation time of 50 seconds or more, more preferably 80 seconds or more, further preferably 100 seconds or more, and may be 150 seconds or more.
  • the stress relaxation time is a value measured by the following method. The stress relaxation time of the above stretched product was measured by connecting both ends of the stretched product to a fixture and tightening the sample to a length of 8 inches (20 cm), keeping the oven at 390 ° C. Insert the fixture into the oven through the slit. The time required for the sample to break from the time of insertion into the oven is defined as the stress relaxation time.
  • the stretched body of the present disclosure preferably has an endothermic peak temperature of 325 to 350 ° C. Further, it is preferable that the stretched body of the present disclosure has an endothermic peak temperature between 325 and 350 ° C and between 360 and 390 ° C.
  • the endothermic peak temperature is a temperature corresponding to the maximum value in the heat of fusion curve when the stretched body is heated at a rate of 10 ° C./min using a differential scanning calorimeter [DSC].
  • the stretched body of the present disclosure preferably has a porosity in the range of 30% to 99%.
  • the porosity is more preferably 40% or more, further preferably 50% or more, further preferably 60% or more, particularly preferably 70% or more. If the proportion of PTFE in the stretched body is too small, the strength of the stretched body may be insufficient, so the porosity is preferably 95% or less, more preferably 90% or less.
  • the method for measuring the density ⁇ of the stretched body is the same as the method described above.
  • the content of the polymer (I) is preferably 0.0001% by mass or more and 20% by mass or less based on polytetrafluoroethylene.
  • the lower limit of the content of the polymer (I) is more preferably 0.001% by mass, further preferably 0.01% by mass, and 0.1% by mass with respect to polytetrafluoroethylene.
  • the upper limit is more preferably 10% by mass, further preferably 6% by mass, even more preferably 4% by mass, particularly preferably 2% by mass or less, particularly preferably 1.5% by mass or less, and 1% by mass or less.
  • the content of the polymer (I) is determined by solid-state NMR measurement.
  • the stretched product of the present disclosure preferably contains substantially no fluorine-containing surfactant.
  • the phrase “substantially free of a fluorine-containing surfactant” means that the fluorine-containing surfactant is 1 mass ppm or less based on polytetrafluoroethylene.
  • the content of the fluorinated surfactant is preferably 100 mass ppb or less, more preferably 10 mass ppb or less, further preferably 1 mass ppb or less, and particularly preferably liquid chromatography-mass spectrometry.
  • the fluorine-containing surfactant is below the detection limit as measured by (LC / MS).
  • the above-mentioned fluorine-containing surfactant is a surfactant containing a fluorine atom having a molecular weight of 800 or less.
  • the fluorinated surfactant include the fluorinated surfactant described in the composition of the present disclosure.
  • fluorine-containing surfactants having a LogPOW of 3.5 or less such as carboxylic acid-based surfactants and sulfonic acid-based surfactants
  • these surfactants are generally Perfluorocarboxylic acid (I) represented by formula (I), ⁇ -H perfluorocarboxylic acid (II) represented by general formula (II), Perfluoropolyether carboxylic acid represented by general formula (III)
  • the stretched body of the present disclosure can be obtained by stretching the composition of the present disclosure.
  • the stretched body of the present disclosure has a shape of a membrane, tube, fiber, or rod.
  • the stretched body of the present disclosure is a membrane (stretched membrane or porous membrane), it can be stretched by a known PTFE stretching method.
  • a uniaxially stretched film can be obtained by roll-stretching a sheet-shaped or rod-shaped paste extrudate in the extrusion direction.
  • a biaxially stretched film can be obtained by stretching the film in the width direction with a tenter or the like. It is also preferable to perform a semi-baking treatment before stretching.
  • the stretched body of the present disclosure is a porous body having a high porosity, and can be suitably used as a filter material for various microfiltration filters such as air filters and chemical liquid filters, and a support material for polymer electrolyte membranes.
  • a filter material for various microfiltration filters such as air filters and chemical liquid filters
  • a support material for polymer electrolyte membranes such as polymer electrolyte membranes.
  • it is also useful as a material for products used in the fields of textiles, medical fields, electrochemical fields, sealing fields, air filtration fields, ventilation / internal pressure adjustment fields, liquid filtration fields, general consumer products fields and the like. The specific uses are illustrated below.
  • Electrochemical field Dielectric material prepreg EMI shielding material, heat transfer material, etc. More specifically, printed wiring boards, electromagnetic shield materials, insulating heat transfer materials, insulating materials, etc. Seal material field Gaskets, packings, pump diaphragms, pump tubes, seal materials for aircraft, etc.
  • Air filtration field ULPA filter for semiconductor manufacturing
  • HEPA filter for hospital and semiconductor manufacturing
  • cylindrical cartridge filter for industrial use
  • bag filter for industrial use
  • heat-resistant bag filter for exhaust gas treatment
  • heat-resistant pleated filter Exhaust gas treatment
  • SINBRAN filter for industrial use
  • catalyst filter for exhaust gas treatment
  • adsorbent filter for HDD incorporation
  • adsorbent vent filter for HDD incorporation
  • vent filter for HDD incorporation, etc.
  • cleaning Machine filters for vacuum cleaners
  • general-purpose multi-layer felt materials for GT cartridge filters (for compatible products for GT), cooling filters (for electronic device housings), etc.
  • Ventilation / Internal pressure adjustment field Freeze-drying materials such as freeze-drying containers, automotive ventilation materials for electronic circuits and lamps, container applications such as container caps, electronic devices including small terminals such as tablet terminals and mobile phone terminals Protective ventilation applications for medical devices, medical ventilation applications, etc.
  • Liquid filtration field Semiconductor liquid filtration filter (for semiconductor production), hydrophilic PTFE filter (for semiconductor production), chemical filter (for chemical treatment), pure water production line filter (for pure water production), backwash liquid Filtration filter (for industrial wastewater treatment), etc.
  • Textile field PTFE fiber fiber material
  • sewing thread textile
  • woven thread textile
  • rope etc.
  • the average primary particle diameter aqueous dispersion was diluted with water to a solid content concentration of 0.15% by mass, and the transmittance of 550 nm projection light per unit length of the obtained diluted latex and transmission electron micrograph
  • the number standard length average primary particle diameter determined by measuring the unidirectional diameter was measured to prepare a calibration curve. Using this calibration curve, the average primary particle diameter was determined from the measured transmittance of 550 nm projected light of each sample.
  • the average primary particle size can be measured by the dynamic light scattering method.
  • a fluoropolymer aqueous dispersion prepared by adjusting the fluoropolymer solid content concentration to about 1.0% by mass was prepared, and using ELSZ-1000S (manufactured by Otsuka Electronics Co., Ltd.) at 25 ° C., a total of 70 times. It was measured at.
  • the refractive index of the solvent (water) is 1.3328, and the viscosity of the solvent (water) is 0.8878 mPa ⁇ s.
  • Standard specific gravity Using a sample molded according to ASTM D 4895 89, it was measured by a water displacement method according to ASTM D 792.
  • Endothermic peak temperature Regarding the PTFE powders obtained in the examples, using a differential scanning calorimeter [DSC], a heat of fusion curve was drawn under the conditions of a temperature rising rate of 10 ° C./min. The temperature corresponding to the maximum value was defined as the endothermic peak temperature of PTFE.
  • the content of PMVE unit was determined from the spectrum obtained by solid state 19 F-MAS NMR measurement using the following formula.
  • the extrusion pressure was determined by the following method according to the method described in JP-A-2002-201217. 21.7 g of a lubricant (trade name: Isopar H (registered trademark), manufactured by Exxon) is added to 100 g of the PTFE powder obtained in the example, and mixed in a glass bottle at room temperature for 3 minutes. The glass bottle is then left at room temperature (25 ° C) for at least 1 hour before extrusion to obtain the lubricated resin. The lubricant resin is extruded through an orifice (diameter: 2.5 mm, land length: 11 mm, introduction angle: 30 °) at room temperature at a reduction ratio of 100: 1 to obtain a uniform beading.
  • a lubricant trade name: Isopar H (registered trademark), manufactured by Exxon
  • the extrusion speed is 20 inches / minute (51 cm / minute).
  • the extrusion pressure is a value obtained by measuring the load when the extrusion load is in an equilibrium state in paste extrusion and dividing by the cross-sectional area of the cylinder used for paste extrusion.
  • This stretching method essentially follows the method disclosed in US Pat. No. 4,576,869, except that the extrusion speed (51 cm / min instead of 84 cm / min) is different.
  • "Stretch" is an increase in length due to stretching and is usually expressed as a ratio to the original length. In the above manufacturing method, the stretching speed is 1000% / sec, and the total stretching is 2400%.
  • Breaking strength A The stretched bead obtained in Stretching test A (made by stretching the bead) was clamped and fixed in a movable jaw having a gauge length of 5.0 cm, and a tensile test was performed at 25 ° C. at a speed of 300 mm / min. The strength at break was measured as the breaking strength A.
  • Breaking strength B A stretched bead was obtained in the same manner as in the stretch test A, except that the clamp interval was 2.0 inches (51 mm) and the stretch speed was changed to 100% / sec. Breaking strength B was measured in the same manner as breaking strength A except that the obtained stretched bead was used.
  • Breaking strength C The wet PTFE powder obtained in the example was dried at 240 ° C. for 18 hours to obtain PTFE powder.
  • the breaking strength C was measured in the same manner as the breaking strength A except that the obtained PTFE powder was used.
  • Breaking strength D The wet PTFE powder obtained in the example was dried at 240 ° C. for 18 hours to obtain PTFE powder. Using the obtained PTFE powder, the breaking strength D was measured in the same manner as the breaking strength A except that the clamp interval was changed to 2.0 inches (51 mm) in the stretching test and the stretching speed was changed to 100% / sec. Was measured.
  • Stretched Body The appearance of the stretched bead obtained in Stretching Test A (produced by stretching the bead) is visually observed. Uniform: The appearance of the stretched beads was uniform. Non-uniformity: The appearance of the stretched bead was non-uniform, such as cracks, swelling and sparseness of the stretched bead.
  • Aqueous dispersion diluted to have an aspect ratio solid content concentration of about 1% by mass was observed with a scanning electron microscope (SEM), and image processing was performed on 400 or more randomly extracted particles to determine their long and short diameters. It was calculated from the average diameter ratio.
  • SEM scanning electron microscope
  • the liquid extract was analyzed using a liquid chromatograph mass spectrometer (Waters, LC-MS ACQUITY UPLC / TQD) to obtain a chromatogram of the liquid extract.
  • the limit of quantification in this measuring instrument configuration is 1 ng / mL.
  • THF tetrahydrofuran
  • Example 1 Into a SUS reactor with a stirrer having an internal volume of 6 L, 3560 g of deionized water, 104 g of paraffin wax, 5.37 g of polymer A and 77.3 mg of modified monomer a were placed. Aqueous ammonia was added to adjust the pH to 9.1. Next, while the contents of the reactor were heated to 70 ° C. and sucked, the contents of the reactor were stirred by purging with TFE to remove oxygen in the reactor. After adding 0.8 g of HFP into the reactor, TFE was added until the pressure reached 0.73 MPaG.
  • ammonium persulfate (APS) initiator dissolved in 20 g deionized water was injected into the reactor and the reactor was brought to a pressure of 0.83 MPaG. A drop in pressure occurred after injection of the initiator and the initiation of polymerization was observed.
  • TFE was added to the reactor to keep the pressure constant at 0.78 MPaG. When the TFE consumed in the reaction reached about 180 g, the feeding and stirring of TFE were stopped. Subsequently, the gas in the reactor was slowly released until the pressure in the reactor reached 0.02 MPaG. Then, TFE was supplied until the pressure of the reactor reached 0.78 MPaG, stirring was started again, and the reaction was continued.
  • APS ammonium persulfate
  • the obtained PTFE aqueous dispersion was diluted with deionized water to a solid content concentration of about 10% by mass, coagulated under high-speed stirring conditions, and the coagulated wet powder was dried at 210 ° C. for 18 hours.
  • Various physical properties of the obtained PTFE powder were measured. The results are shown in the table.
  • Example 2 Polymerization was performed in the same manner as in Example 2 except that 77.3 mg of the modified monomer a in Example 1 was 9.7 mg and 0.8 g of HFP was 0.27 g of PMVE.
  • the solid content concentration of the obtained PTFE aqueous dispersion was 24.4% by mass, and the average primary particle diameter was 275 nm.
  • PTFE powder was obtained in the same manner as in Example 1, and various physical properties of the obtained PTFE powder were measured. The results are shown in the table.
  • Example 3 Polymerization was performed in the same manner as in Example 1 except that 14.3 mg of hydroquinone in Example 1 was not injected into the reactor.
  • the solid content concentration of the obtained PTFE aqueous dispersion was 25.4% by mass, and the average primary particle diameter was 242 nm.
  • PTFE powder was obtained in the same manner as in Example 1, and various physical properties of the obtained PTFE powder were measured. The results are shown in the table.
  • Example 4 1800 g of deionized water, 90 g of paraffin wax, 2.70 g of polymer A and 38.9 mg of modified monomer a were placed in a SUS reactor with a stirrer having an internal capacity of 3 L. Aqueous ammonia was added to adjust the pH to 9.1. Next, while the contents of the reactor were heated to 80 ° C. and sucked, at the same time, TFE was purged to remove oxygen in the reactor, and the contents were stirred. After adding 2.3 g of HFP into the reactor, TFE was added until the pressure reached 1.50 MPaG. 9.0 mg of ammonium persulfate (APS) initiator was injected into the reactor.
  • APS ammonium persulfate
  • TFE was added to the reactor to keep the pressure constant at 1.50 MPaG.
  • the TFE supply and stirring were stopped.
  • the gas in the reactor was slowly released until the pressure in the reactor reached atmospheric pressure, and the vacuum was further maintained for 1 minute.
  • TFE was supplied until the pressure of the reactor reached 2.50 MPaG, stirring was started again, and the reaction was continued.
  • the TFE consumed in the reaction reached about 180 g, 14.4 mg of hydroquinone dissolved in 20 g of deionized water was injected into the reactor, and the reaction was continued.
  • the TFE consumed in the reaction reached about 600 g
  • the supply of TFE was stopped, stirring was stopped, and the reaction was completed.
  • the pressure in the reactor was evacuated to normal pressure, and the contents were taken out from the reactor and cooled.
  • the supernatant paraffin wax was removed from the PTFE aqueous dispersion.
  • the solid content concentration of the obtained PTFE aqueous dispersion was 26.9% by mass, and the average primary particle diameter was 196 nm.
  • the obtained PTFE aqueous dispersion was diluted with deionized water to a solid content concentration of about 10% by mass, coagulated under high-speed stirring conditions, and the coagulated wet powder was dried at 210 ° C. for 18 hours.
  • Various physical properties of the obtained PTFE powder were measured. The results are shown in the table.
  • Preparation example 1 To the reactor, 220 g of a monomer D represented by CH 2 ⁇ CF (CF 2 OCFCF 3 COOH) and 513 g of water were added, and further 0.5 mol% of ammonium persulfate (APS) was added to the monomer D. . The mixture was heated and stirred at 60 ° C. for 24 hours in a nitrogen atmosphere to obtain a polymer D aqueous solution D-1 containing a polymer D which was a homopolymer of CH 2 ⁇ CF (CF 2 OCFCF 3 COOH). As a result of GPC analysis of the obtained polymer D aqueous solution D-1, the content of Mw 180,000, Mn 86,000, dimer, and trimer was 2.0% by mass with respect to the polymer D. there were.
  • APS ammonium persulfate
  • the content of Mw 180,000, Mn 140,000, dimer, and trimer was less than 1 ppm with respect to the polymer D.
  • the concentration of the resulting polymer D aqueous solution D-2 was 5.0% by mass.
  • Example 5 In a SUS reactor with a stirrer having an internal volume of 6 L, 3457 g of deionized water, 180 g of paraffin wax, 107.4 g of a polymer D aqueous solution D-2, and 1.1 g of a 1.0 mass% isopropanol aqueous solution were added. I put it in. Aqueous ammonia was added to adjust the pH to 9.1. Next, while the contents of the reactor were heated to 70 ° C. and sucked, the contents of the reactor were stirred by purging with TFE to remove oxygen in the reactor. After adding 0.54 g of PMVE into the reactor, TFE was added until the pressure reached 0.73 MPaG.
  • ammonium persulfate (APS) initiator dissolved in 20 g deionized water was injected into the reactor and the reactor was brought to a pressure of 0.83 MPaG. A drop in pressure occurred after injection of the initiator and the initiation of polymerization was observed.
  • TFE was added to the reactor to keep the pressure constant at 0.78 MPaG. When the TFE consumed in the reaction reached about 180 g, the feeding and stirring of TFE were stopped. Subsequently, the gas in the reactor was slowly released until the pressure in the reactor reached 0.02 MPaG. Then, TFE was supplied until the pressure of the reactor reached 0.78 MPaG, stirring was started again, and the reaction was continued.
  • APS ammonium persulfate
  • the obtained PTFE aqueous dispersion was diluted with deionized water to a solid content concentration of about 10% by mass, coagulated under high-speed stirring conditions, and the coagulated wet powder was dried at 210 ° C. for 18 hours.
  • Various physical properties of the obtained PTFE powder were measured. The results are shown in the table.
  • Example 6 Polymerization was carried out in the same manner as in Example 5 except that the amount of the isopropanol aqueous solution added was changed to 2.1 g. Various physical properties of the obtained PTFE aqueous dispersion were measured. The results are shown in the table. PTFE powder was obtained in the same manner as in Example 5, and various physical properties of the obtained PTFE powder were measured. The results are shown in the table.
  • Example 7 Same as Example 5 except that the aqueous solution of isopropanol was changed to 1.8 g of 0.1% by mass concentration of Triton X-100 (trade name, manufactured by Dow Chemical Co.) (hereinafter referred to as "Triton aqueous solution”). Was polymerized. Various physical properties of the obtained PTFE aqueous dispersion were measured. The results are shown in the table. PTFE powder was obtained in the same manner as in Example 5, and various physical properties of the obtained PTFE powder were measured. The results are shown in the table.
  • Example 8 Polymerization was performed in the same manner as in Example 5 except that 0.9 g of a 0.1% by mass concentration Triton aqueous solution was further added to the reactor together with the isopropanol aqueous solution. Various physical properties of the obtained PTFE aqueous dispersion were measured. The results are shown in the table. PTFE powder was obtained in the same manner as in Example 5, and various physical properties of the obtained PTFE powder were measured. The results are shown in the table. In addition, the measurement results of breaking strength are shown in the table.
  • Example 9 Polymerization was carried out in the same manner as in Example 5 except that 1.8 g of a 0.1 mass% Triton aqueous solution was further added to the reactor together with the isopropanol aqueous solution. Various physical properties of the obtained PTFE aqueous dispersion were measured. The results are shown in the table. PTFE powder was obtained in the same manner as in Example 5, and various physical properties of the obtained PTFE powder were measured. The results are shown in the table.
  • Example 10 Polymerization was carried out in the same manner as in Example 5 except that PMVE was changed to 2.4 g of HFP. Various physical properties of the obtained PTFE aqueous dispersion were measured. The results are shown in the table. PTFE powder was obtained in the same manner as in Example 5, and various physical properties of the obtained PTFE powder were measured. The results are shown in the table.
  • Example 11 Polymerization was carried out in the same manner as in Example 10 except that 1.8 g of 0.1% by mass concentration of Triton aqueous solution was further added to the reactor together with the isopropanol aqueous solution. Various physical properties of the obtained PTFE aqueous dispersion were measured. The results are shown in the table. PTFE powder was obtained in the same manner as in Example 5, and various physical properties of the obtained PTFE powder were measured. The results are shown in the table.
  • Example 12 The Triton aqueous solution put in the reactor was changed to 1.25 g of the Triton aqueous solution having a concentration of 0.1% by mass, the amount of PMVE added was changed to 0.27 g, and when the TFE consumed in the reaction reached about 180 g, Polymerization was performed in the same manner as in Example 8 except that the pressure was kept constant without stopping the supply and stirring of TFE. Various physical properties of the obtained PTFE aqueous dispersion were measured. The results are shown in the table. PTFE powder was obtained in the same manner as in Example 5, and various physical properties of the obtained PTFE powder were measured. The results are shown in the table.
  • Example 13 Polymerization was performed in the same manner as in Example 5 except that the isopropanol aqueous solution was not placed in the reactor. Various physical properties of the obtained PTFE aqueous dispersion were measured. The results are shown in the table.
  • PTFE powder was obtained in the same manner as in Example 5, and various physical properties of the obtained PTFE powder were measured. The results are shown in the table.

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Abstract

L'invention fournit une composition qui est caractéristique en ce qu'elle contient un polytétrafluoréthylène, et un polymère (I) contenant une unité polymère (I) basée sur un monomère représenté par la formule générale (I), et en ce que sa densité standard est inférieure ou égale à 2,200. ＣＸ１Ｘ３＝ＣＸ２Ｒ（－ＣＺ１Ｚ２－Ａ０）ｍ　（Ｉ） (Dans la formule, Ｘ１ et Ｘ３ représentent chacun indépendamment Ｆ, Ｃｌ, Ｈ ou ＣＦ３; Ａ０ représente un groupe aninique; Ｘ２ représente H, F, un groupe alkyle ou un groupe alkyle fluoré; R représente un groupe de liaison; Ｚ１ et Ｚ２ représentent chacun indépendamment H, F, un groupe alkyle ou un groupe alkyle fluoré; et m représente un nombre entier supérieur ou égal à 1).
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Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2021100835A1 (fr) * 2019-11-19 2021-05-27 ダイキン工業株式会社 Procédé de fabrication de fluoropolymère
WO2021100836A1 (fr) * 2019-11-19 2021-05-27 ダイキン工業株式会社 Procédé de production de fluoropolymère, procédé de production de polytétrafluoroéthylène, procédé de production de perfluoroélastomère et composition
EP3760649A4 (fr) * 2018-03-01 2021-12-29 Daikin Industries, Ltd. Procédé de fabrication de fluoropolymère
WO2022244785A1 (fr) * 2021-05-19 2022-11-24 ダイキン工業株式会社 Fluoropolymère, solution aqueuse et composition de revêtement
EP4026856A4 (fr) * 2019-09-05 2023-09-27 Daikin Industries, Ltd. Procédé de fabrication de perfluoroélastomère, et composition
WO2023210820A1 (fr) * 2022-04-28 2023-11-02 ダイキン工業株式会社 Procédé de production d'une composition contenant une résine fluorée, et composition contenant une résine fluorée
EP4063405A4 (fr) * 2019-11-19 2024-01-10 Daikin Industries, Ltd. Procédé de production de polytétrafluoroéthylène
WO2024034675A1 (fr) * 2022-08-10 2024-02-15 ダイキン工業株式会社 Polytétrafluoroéthylène modifié, et corps étiré

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113774502B (zh) * 2021-09-08 2022-09-06 深圳市明鑫高分子技术有限公司 一种高频稳相的ptfe膜材料及其制造方法

Citations (54)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3250808A (en) 1963-10-31 1966-05-10 Du Pont Fluorocarbon ethers derived from hexafluoropropylene epoxide
US3271341A (en) 1961-08-07 1966-09-06 Du Pont Aqueous colloidal dispersions of polymer
US3391099A (en) 1966-04-25 1968-07-02 Du Pont Polymerization process
US4576869A (en) 1984-06-18 1986-03-18 E. I. Du Pont De Nemours And Company Tetrafluoroethylene fine powder and preparation thereof
JPS61293476A (ja) 1984-12-26 1986-12-24 エルフ　アトケム　ソシエテ　アノニム 親水性基を有するフツ素化テロマ−含有消火用乳化剤
WO1987007619A1 (fr) 1986-06-13 1987-12-17 Societe Chimique Des Charbonnages S.A. Procede d'agglomeration d'un latex
WO1992017635A1 (fr) 1991-04-02 1992-10-15 Minnesota Mining And Manufacturing Company Derives d'isocyanate comprenant des oligomeres fluorochimiques
JPH11181009A (ja) 1997-12-22 1999-07-06 Asahi Glass Co Ltd ポリテトラフルオロエチレンの棒状微粒子を含む水性分散液の製造方法
JP2001226436A (ja) 2000-02-16 2001-08-21 Daikin Ind Ltd フッ素系アイオノマー共重合体の製造法
JP2002517537A (ja) * 1998-05-29 2002-06-18 イー・アイ・デュポン・ドウ・ヌムール・アンド・カンパニー 染色できるフルオロ重合体の繊維及びフィルム
JP2002201217A (ja) 2000-10-30 2002-07-19 Asahi Glass Co Ltd 強度に優れるテトラフルオロエチレン重合体
JP2003119204A (ja) 2001-10-05 2003-04-23 Daikin Ind Ltd 含フッ素重合体ラテックスの製造方法
JP2004075978A (ja) 2002-06-17 2004-03-11 Daikin Ind Ltd 含フッ素結晶性ポリマー分散体製造方法
WO2004067588A1 (fr) 2003-01-24 2004-08-12 3M Innovative Properties Company Polymerization en emulsion de monomeres fluores
US6841616B2 (en) 2003-03-28 2005-01-11 Arkema Inc. Polymerization of halogen-containing monomers using siloxane surfactant
US6841594B2 (en) 2002-01-04 2005-01-11 E. I. Du Pont De Nemours And Company Core-shell fluoropolymer dispersions
WO2005042593A1 (fr) 2003-10-31 2005-05-12 Daikin Industries, Ltd. Procede de production d'une dispersion aqueuse de fluoropolymere, et dispersion aqueuse de fluoropolymere
JP2005320501A (ja) * 2004-04-07 2005-11-17 Daikin Ind Ltd 含フッ素エラストマー重合体の製造方法
WO2006119224A1 (fr) 2005-05-03 2006-11-09 3M Innovative Properties Company Ionomeres fluores avec des quantites reduites de groupes terminaux carbonyles
WO2006135825A1 (fr) 2005-06-10 2006-12-21 3M Innovative Properties Company Polymerisation sous emulsion aqueuse de monomeres fluores en presence d'oligomere partiellement fluore comme emulsifiant
US20070015865A1 (en) 2005-07-15 2007-01-18 3M Innovative Properties Company Aqueous emulsion polymerization of fluorinated monomers using a perfluoropolyether surfactant
US20070015864A1 (en) 2005-07-15 2007-01-18 3M Innovative Properties Company Method of making fluoropolymer dispersion
US20070015866A1 (en) 2005-07-15 2007-01-18 3M Innovative Properties Company Aqueous emulsion polymerization of fluorinated monomers using a fluorinated surfactant
WO2007046377A1 (fr) 2005-10-20 2007-04-26 Asahi Glass Company, Limited Procédé servant à produire une résine fluorée pouvant être moulée à l'état fondu
WO2007046345A1 (fr) 2005-10-17 2007-04-26 Asahi Glass Company, Limited Emulsion aqueuse de polytetrafluoroethylene et poudre fine de polytetrafluoroethylene et materiau poreux produit a partir de celle-ci
WO2007046482A1 (fr) 2005-10-20 2007-04-26 Asahi Glass Company, Limited Dispersion aqueuse de polytétrafluoroéthylène et produit formé à partir de celle-ci
US20070117914A1 (en) 2005-11-24 2007-05-24 3M Innovative Properties Company Fluorinated surfactants for use in making a fluoropolymer
US20070142541A1 (en) 2005-12-21 2007-06-21 3M Innovative Properties Company Fluorinated surfactants for making fluoropolymers
WO2007119526A1 (fr) 2006-04-14 2007-10-25 Bridgestone Corporation Appareil chauffant en ligne et son procede de fabrication
US20070276103A1 (en) 2006-05-25 2007-11-29 3M Innovative Properties Company Fluorinated Surfactants
US20080015319A1 (en) 2006-07-13 2008-01-17 Klaus Hintzer Explosion taming surfactants for the production of perfluoropolymers
WO2008060461A1 (fr) 2006-11-09 2008-05-22 E. I. Du Pont De Nemours And Company Polymérisation aqueuse de monomère fluoré faisant intervenir un agent de polymérisation comprenant un acide de fluoropolyéther ou un sel de celui-ci et un fluorotensioactif à chaîne courte
WO2009055521A1 (fr) 2007-10-23 2009-04-30 Dupont Performance Elastomers L.L.C. Oligomères dysfonctionnels du perfluoro(méthylvinyléther)
WO2009068528A1 (fr) 2007-11-26 2009-06-04 Solvay Solexis S.P.A. Composition liquide d'ionomère fluoré
JP2009539049A (ja) * 2006-05-31 2009-11-12 イー・アイ・デュポン・ドウ・ヌムール・アンド・カンパニー アニオン性高分子電解質分散剤で安定化されたフルオロポリマー分散液からのフィラー入りベアリングの形成方法
WO2010075496A1 (fr) 2008-12-23 2010-07-01 E. I. Du Pont De Nemours And Company Polymère fluoré produit par une polymérisation aqueuse utilisant des particules dispersées d'un ionomère fluoré produit in situ
WO2010075494A1 (fr) 2008-12-23 2010-07-01 E. I. Du Pont De Nemours And Company Particules de fluoropolymère comprenant un noyau d'ionomère fluoré
WO2010075497A1 (fr) 2008-12-23 2010-07-01 E. I. Du Pont De Nemours And Company Ionomère fluoré produit par une polymérisation aqueuse utilisant des particules dispersées d'un ionomère fluoré produit in situ
WO2010075359A1 (fr) 2008-12-23 2010-07-01 E. I. Du Pont De Nemours And Company Polymère fluoré obtenu par polymérisation aqueuse à l'aide de particules dispersées d'ionomère fluoré
WO2011008381A1 (fr) 2009-07-16 2011-01-20 Dupont Performance Elastomers L.L.C. Polymères fluorés à terminaisons diacrylate
WO2011014715A2 (fr) 2009-07-31 2011-02-03 3M Innovative Properties Company Compositions de fluoropolymère contenant un composé polyol et leurs procédés de fabrication
WO2012082703A2 (fr) 2010-12-17 2012-06-21 3M Innovative Properties Company Préparation d'oligomères et de co-oligomères d'acides sulfiniques hautement fluorés et de sels de ceux-ci
WO2012082451A2 (fr) 2010-12-17 2012-06-21 3M Innovative Properties Company Oligomères fluorés ayant des fractions contenant du brome pendantes
WO2012082454A1 (fr) 2010-12-17 2012-06-21 3M Innovative Properties Company Oligomères et co-oligomères d'acide sulfinique hautement fluoré et leurs sels
WO2012082707A1 (fr) 2010-12-17 2012-06-21 3M Innovative Properties Company Microémulsions et polymères fluorés fabriqués à l'aide des microémulsions
WO2013085864A2 (fr) 2011-12-06 2013-06-13 3M Innovative Properties Company Oligomères fluorés ayant des groupes fonctionnels latéraux
WO2013146950A1 (fr) 2012-03-30 2013-10-03 ダイキン工業株式会社 Composition d'agent tensio-actif non ionique et dispersion aqueuse de polymère fluoré
WO2013146947A1 (fr) 2012-03-27 2013-10-03 ダイキン工業株式会社 Dispersion aqueuse de polymère fluoré
WO2013189826A1 (fr) 2012-06-20 2013-12-27 Solvay Specialty Polymers Italy S.P.A. Copolymères de tétrafluoroéthylène
WO2013189824A1 (fr) 2012-06-20 2013-12-27 Solvay Specialty Polymers Italy S.P.A. Copolymères de tétrafluoroéthylène
WO2014069165A1 (fr) 2012-10-29 2014-05-08 旭硝子株式会社 Procédé de préparation d'un copolymère fluoré
WO2014099453A1 (fr) 2012-12-18 2014-06-26 E. I. Du Pont De Nemours And Company Procédé de production de fluoroélastomères
US20140228531A1 (en) 2008-07-08 2014-08-14 Solvay Solexis S.P.A. Method for manufacturing fluoropolymers
WO2019168183A1 (fr) * 2018-03-01 2019-09-06 ダイキン工業株式会社 Procédé de fabrication de fluoropolymère

Family Cites Families (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5670593A (en) * 1994-06-09 1997-09-23 Daikin Industries, Ltd. Fluorine-containing olefin, fluorine-containing polymer and thermoplastic resin composition prepared by using said polymer
EP1201689B1 (fr) * 2000-10-30 2008-09-24 Asahi Glass Company, Limited Tetrafluoroéthylène polymère pour étirement
JP4233276B2 (ja) * 2002-06-27 2009-03-04 三井・デュポンフロロケミカル株式会社 電極材料用結着剤
WO2008111528A1 (fr) * 2007-03-07 2008-09-18 Nec Corporation Pile à combustible
JP2010132712A (ja) * 2007-03-13 2010-06-17 Daikin Ind Ltd 多孔体及びフィルター
JP5607435B2 (ja) * 2010-06-18 2014-10-15 旭化成イーマテリアルズ株式会社 電解質膜並びにその製造方法、電極触媒層並びにその製造方法、膜電極接合体、及び、固体高分子電解質型燃料電池
WO2015083790A1 (fr) * 2013-12-06 2015-06-11 ダイキン工業株式会社 Séparateur pour batterie secondaire et batterie secondaire
US20220002531A1 (en) * 2018-11-19 2022-01-06 Daikin Industries, Ltd. Production method of modified polytetrafluoroethylene and composition

Patent Citations (56)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3271341A (en) 1961-08-07 1966-09-06 Du Pont Aqueous colloidal dispersions of polymer
US3250808A (en) 1963-10-31 1966-05-10 Du Pont Fluorocarbon ethers derived from hexafluoropropylene epoxide
US3391099A (en) 1966-04-25 1968-07-02 Du Pont Polymerization process
US4576869A (en) 1984-06-18 1986-03-18 E. I. Du Pont De Nemours And Company Tetrafluoroethylene fine powder and preparation thereof
JPS61293476A (ja) 1984-12-26 1986-12-24 エルフ　アトケム　ソシエテ　アノニム 親水性基を有するフツ素化テロマ−含有消火用乳化剤
WO1987007619A1 (fr) 1986-06-13 1987-12-17 Societe Chimique Des Charbonnages S.A. Procede d'agglomeration d'un latex
WO1992017635A1 (fr) 1991-04-02 1992-10-15 Minnesota Mining And Manufacturing Company Derives d'isocyanate comprenant des oligomeres fluorochimiques
JPH11181009A (ja) 1997-12-22 1999-07-06 Asahi Glass Co Ltd ポリテトラフルオロエチレンの棒状微粒子を含む水性分散液の製造方法
JP2002517537A (ja) * 1998-05-29 2002-06-18 イー・アイ・デュポン・ドウ・ヌムール・アンド・カンパニー 染色できるフルオロ重合体の繊維及びフィルム
JP2001226436A (ja) 2000-02-16 2001-08-21 Daikin Ind Ltd フッ素系アイオノマー共重合体の製造法
JP2002201217A (ja) 2000-10-30 2002-07-19 Asahi Glass Co Ltd 強度に優れるテトラフルオロエチレン重合体
JP2003119204A (ja) 2001-10-05 2003-04-23 Daikin Ind Ltd 含フッ素重合体ラテックスの製造方法
US6841594B2 (en) 2002-01-04 2005-01-11 E. I. Du Pont De Nemours And Company Core-shell fluoropolymer dispersions
JP2004075978A (ja) 2002-06-17 2004-03-11 Daikin Ind Ltd 含フッ素結晶性ポリマー分散体製造方法
WO2004067588A1 (fr) 2003-01-24 2004-08-12 3M Innovative Properties Company Polymerization en emulsion de monomeres fluores
US6841616B2 (en) 2003-03-28 2005-01-11 Arkema Inc. Polymerization of halogen-containing monomers using siloxane surfactant
WO2005042593A1 (fr) 2003-10-31 2005-05-12 Daikin Industries, Ltd. Procede de production d'une dispersion aqueuse de fluoropolymere, et dispersion aqueuse de fluoropolymere
JP2005320501A (ja) * 2004-04-07 2005-11-17 Daikin Ind Ltd 含フッ素エラストマー重合体の製造方法
WO2006119224A1 (fr) 2005-05-03 2006-11-09 3M Innovative Properties Company Ionomeres fluores avec des quantites reduites de groupes terminaux carbonyles
WO2006135825A1 (fr) 2005-06-10 2006-12-21 3M Innovative Properties Company Polymerisation sous emulsion aqueuse de monomeres fluores en presence d'oligomere partiellement fluore comme emulsifiant
JP2008545873A (ja) * 2005-06-10 2008-12-18 スリーエム イノベイティブ プロパティズ カンパニー 乳化剤としての部分フッ素化されたオリゴマーの存在下におけるフッ素化モノマーの水性エマルション重合
US20070015866A1 (en) 2005-07-15 2007-01-18 3M Innovative Properties Company Aqueous emulsion polymerization of fluorinated monomers using a fluorinated surfactant
US20070015864A1 (en) 2005-07-15 2007-01-18 3M Innovative Properties Company Method of making fluoropolymer dispersion
US20070015865A1 (en) 2005-07-15 2007-01-18 3M Innovative Properties Company Aqueous emulsion polymerization of fluorinated monomers using a perfluoropolyether surfactant
WO2007046345A1 (fr) 2005-10-17 2007-04-26 Asahi Glass Company, Limited Emulsion aqueuse de polytetrafluoroethylene et poudre fine de polytetrafluoroethylene et materiau poreux produit a partir de celle-ci
WO2007046377A1 (fr) 2005-10-20 2007-04-26 Asahi Glass Company, Limited Procédé servant à produire une résine fluorée pouvant être moulée à l'état fondu
WO2007046482A1 (fr) 2005-10-20 2007-04-26 Asahi Glass Company, Limited Dispersion aqueuse de polytétrafluoroéthylène et produit formé à partir de celle-ci
US20070117914A1 (en) 2005-11-24 2007-05-24 3M Innovative Properties Company Fluorinated surfactants for use in making a fluoropolymer
US20070142541A1 (en) 2005-12-21 2007-06-21 3M Innovative Properties Company Fluorinated surfactants for making fluoropolymers
WO2007119526A1 (fr) 2006-04-14 2007-10-25 Bridgestone Corporation Appareil chauffant en ligne et son procede de fabrication
US20070276103A1 (en) 2006-05-25 2007-11-29 3M Innovative Properties Company Fluorinated Surfactants
JP2009539049A (ja) * 2006-05-31 2009-11-12 イー・アイ・デュポン・ドウ・ヌムール・アンド・カンパニー アニオン性高分子電解質分散剤で安定化されたフルオロポリマー分散液からのフィラー入りベアリングの形成方法
US20080015319A1 (en) 2006-07-13 2008-01-17 Klaus Hintzer Explosion taming surfactants for the production of perfluoropolymers
WO2008060461A1 (fr) 2006-11-09 2008-05-22 E. I. Du Pont De Nemours And Company Polymérisation aqueuse de monomère fluoré faisant intervenir un agent de polymérisation comprenant un acide de fluoropolyéther ou un sel de celui-ci et un fluorotensioactif à chaîne courte
WO2009055521A1 (fr) 2007-10-23 2009-04-30 Dupont Performance Elastomers L.L.C. Oligomères dysfonctionnels du perfluoro(méthylvinyléther)
WO2009068528A1 (fr) 2007-11-26 2009-06-04 Solvay Solexis S.P.A. Composition liquide d'ionomère fluoré
US20140228531A1 (en) 2008-07-08 2014-08-14 Solvay Solexis S.P.A. Method for manufacturing fluoropolymers
JP2012513534A (ja) * 2008-12-23 2012-06-14 イー・アイ・デュポン・ドウ・ヌムール・アンド・カンパニー その場生成されるフッ素化イオノマーの分散した微粒子を使用する水性重合によって製造されるフルオロポリマー
WO2010075497A1 (fr) 2008-12-23 2010-07-01 E. I. Du Pont De Nemours And Company Ionomère fluoré produit par une polymérisation aqueuse utilisant des particules dispersées d'un ionomère fluoré produit in situ
WO2010075359A1 (fr) 2008-12-23 2010-07-01 E. I. Du Pont De Nemours And Company Polymère fluoré obtenu par polymérisation aqueuse à l'aide de particules dispersées d'ionomère fluoré
WO2010075494A1 (fr) 2008-12-23 2010-07-01 E. I. Du Pont De Nemours And Company Particules de fluoropolymère comprenant un noyau d'ionomère fluoré
WO2010075496A1 (fr) 2008-12-23 2010-07-01 E. I. Du Pont De Nemours And Company Polymère fluoré produit par une polymérisation aqueuse utilisant des particules dispersées d'un ionomère fluoré produit in situ
WO2011008381A1 (fr) 2009-07-16 2011-01-20 Dupont Performance Elastomers L.L.C. Polymères fluorés à terminaisons diacrylate
WO2011014715A2 (fr) 2009-07-31 2011-02-03 3M Innovative Properties Company Compositions de fluoropolymère contenant un composé polyol et leurs procédés de fabrication
WO2012082707A1 (fr) 2010-12-17 2012-06-21 3M Innovative Properties Company Microémulsions et polymères fluorés fabriqués à l'aide des microémulsions
WO2012082454A1 (fr) 2010-12-17 2012-06-21 3M Innovative Properties Company Oligomères et co-oligomères d'acide sulfinique hautement fluoré et leurs sels
WO2012082451A2 (fr) 2010-12-17 2012-06-21 3M Innovative Properties Company Oligomères fluorés ayant des fractions contenant du brome pendantes
WO2012082703A2 (fr) 2010-12-17 2012-06-21 3M Innovative Properties Company Préparation d'oligomères et de co-oligomères d'acides sulfiniques hautement fluorés et de sels de ceux-ci
WO2013085864A2 (fr) 2011-12-06 2013-06-13 3M Innovative Properties Company Oligomères fluorés ayant des groupes fonctionnels latéraux
WO2013146947A1 (fr) 2012-03-27 2013-10-03 ダイキン工業株式会社 Dispersion aqueuse de polymère fluoré
WO2013146950A1 (fr) 2012-03-30 2013-10-03 ダイキン工業株式会社 Composition d'agent tensio-actif non ionique et dispersion aqueuse de polymère fluoré
WO2013189826A1 (fr) 2012-06-20 2013-12-27 Solvay Specialty Polymers Italy S.P.A. Copolymères de tétrafluoroéthylène
WO2013189824A1 (fr) 2012-06-20 2013-12-27 Solvay Specialty Polymers Italy S.P.A. Copolymères de tétrafluoroéthylène
WO2014069165A1 (fr) 2012-10-29 2014-05-08 旭硝子株式会社 Procédé de préparation d'un copolymère fluoré
WO2014099453A1 (fr) 2012-12-18 2014-06-26 E. I. Du Pont De Nemours And Company Procédé de production de fluoroélastomères
WO2019168183A1 (fr) * 2018-03-01 2019-09-06 ダイキン工業株式会社 Procédé de fabrication de fluoropolymère

Non-Patent Citations (3)

* Cited by examiner, † Cited by third party
Title
KASAI, J. APPL. POLYMER SCI., vol. 57, 1995, pages 797
R.S. M. HILL: "Silicone Surfactants", MARCEL DEKKER, INC.
ROMPP: "Lexikon Chemie", 1999, GEORG THIEME VERLAG

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP3760649A4 (fr) * 2018-03-01 2021-12-29 Daikin Industries, Ltd. Procédé de fabrication de fluoropolymère
US11767379B2 (en) 2018-03-01 2023-09-26 Daikin Industries, Ltd. Method for manufacturing fluoropolymer
EP4026856A4 (fr) * 2019-09-05 2023-09-27 Daikin Industries, Ltd. Procédé de fabrication de perfluoroélastomère, et composition
WO2021100835A1 (fr) * 2019-11-19 2021-05-27 ダイキン工業株式会社 Procédé de fabrication de fluoropolymère
WO2021100836A1 (fr) * 2019-11-19 2021-05-27 ダイキン工業株式会社 Procédé de production de fluoropolymère, procédé de production de polytétrafluoroéthylène, procédé de production de perfluoroélastomère et composition
EP4063405A4 (fr) * 2019-11-19 2024-01-10 Daikin Industries, Ltd. Procédé de production de polytétrafluoroéthylène
EP4063403A4 (fr) * 2019-11-19 2024-01-24 Daikin Industries, Ltd. Procédé de fabrication de fluoropolymère
WO2022244785A1 (fr) * 2021-05-19 2022-11-24 ダイキン工業株式会社 Fluoropolymère, solution aqueuse et composition de revêtement
WO2023210820A1 (fr) * 2022-04-28 2023-11-02 ダイキン工業株式会社 Procédé de production d'une composition contenant une résine fluorée, et composition contenant une résine fluorée
WO2024034675A1 (fr) * 2022-08-10 2024-02-15 ダイキン工業株式会社 Polytétrafluoroéthylène modifié, et corps étiré

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